NOVELTY - The present invention relates to an improved device and process for the production of biodiesel from variety of oil seeds in homes by using a compact model which will require low floor space requirement similar to that of home appliances like washing machine and also cost effective and efficient. This will help all vehicle users to generate fuel required for their personal vehicle, on day to day life. Following invention is described in detail with the help of Figure 1 of sheet 1 which shows process diagram, Figure 2 of sheet 2 shows the whole setup of the product, Figure 3 of sheet 3 shows front view of reactor and Figure 4 of sheet 4 shows top view of the reactor.
NOVELTY - The apparatus (1) has column portion (20) in which herbal biomass which carried out delignification process is filled with an alkali. The column portion is arranged in perpendicular direction in a denitrifying reaction tank (100). The to-be-processed water is supplied to an inside of an upward flow type tank from a lower portion. The herbal biomass is Phragmites or chaff. The filling rate of the Phragmites in the column is 25-65 %, and the filling rate of the chaff in the column is 15-45%.    USE - Apparatus for treating waste water such as waste material reclaimed-ground leachate (claimed) in waste water processing facility. Can also be used in treating organic waste water of nitrogen-containing inorganic type industrial effluent, industrial waste reclaimed-ground leachate, digestive supernatant liquor and nitrification treated water.    ADVANTAGE - Since the addition of the chemical agents for treating the waste water can be avoided, the nitrous acid and nitrate nitrogen in the waste water can be removed efficiently, and the expense of waste water treatment can be lowered, by using the herbal biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a waste-water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows the top view and the side view of the apparatus for treating the waste water. (Drawing includes non-English language text)    Apparatus for treating waste water (1)    Column portion (20)    Denitrifying reaction tank (100)    Partition portion (110)    Treated-water acquisition valve (180)
NOVELTY - A hydrogen generation catalyst comprises mesoporous metal oxide containing 1st catalyst component selected from aluminum, magnesium, lanthanum, barium, calcium, and/or cerium and 2nd catalyst component containing platinum, rhodium, palladium, nickel, and/or cobalt in which 2nd catalyst component is supported by mesoporous metal oxide. Mesoporous metal oxide has pore distribution peak of 5-10 nm.    USE - A hydrogen generation catalyst for system used for producing hydrogen (claimed).    ADVANTAGE - The hydrogen generation catalyst exhibits high activity at low temperature and improves energy efficiency of various devices. The hydrogen generation catalyst-containing system efficiently produces hydrogen at low temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) system which uses hydrogen generation catalyst and produces reformed gas-containing hydrogen by reacting greater than or equal to 1 part of exhaust gas containing water and fuel in the presence of hydrogen generation catalyst; and    (2) manufacture of hydrogen generation catalyst which involves mixing raw material of mesoporous metal oxide, solution comprising 1st catalyst component-containing raw material, and nonionic high molecular weight surface active agent.
NOVELTY - A proton electroconductivity ceramic joined material has strontium cerium oxide-type base which added a bivalent or trivalent cation and a surface layer located on the surface side of the base. The surface layer is formed by screen-printing ink produced by mixing a strontium zirconium oxide powder which added the cation of bivalence or trivalence and an organic solvent.    USE - Proton electroconductivity ceramic joined material used for manufacturing hydrogen and purifying electrolyte of fuel cell.    ADVANTAGE - The ceramic joined material has favorable proton electroconductivity at high temperature even in carbon dioxide atmosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of proton electroconductivity ceramic joined material.
NOVELTY - A mesoporous metal oxide comprises silicon-oxide frame, silicon and cerium.    USE - Mesoporous metal oxide for fuel modification catalyst used for fuel reforming system for generating hydrogen (all claimed).    ADVANTAGE - Low-temperature activity and high temperature durability are excellent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel modification catalyst comprising mesoporous metal oxide, 1st catalyst component containing magnesium, lanthanum, zirconium and niobium which are carried by mesoporous metal oxide, and 2nd catalyst component containing platinum, rhodium, palladium, nickel and cobalt which are carried by mesoporous metal oxide; and    (2) fuel reforming system comprising catalytic reactor containing fuel modification catalyst.
NOVELTY - An ion exchange membrane (1) comprises a membrane main component (10) and a coating layer (11a, 11b) comprising inorganic particles and a binder, provided on surface(s) of the membrane main component. The membrane main component contains a fluorine-containing polymer having an ion exchange group. The specific surface area of the coating layer is 0.1-10 m2/g.    USE - Ion exchange membrane e.g. cation exchange membrane is used for electrolytic cell (claimed) for water electrolysis, hydrochloric acid electrolysis and alkali chloride electrolysis, and used as diaphragm for ozone generation, and for fuel cell.    ADVANTAGE - The ion exchange membrane has stable electrolysis capability, and is free from impurities in electrolyte solution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of ion-exchange membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the ion exchange membrane.    Ion exchange membrane (1)    Sulfonic acid layer (3)    Reinforcement core material (4)    Membrane main component (10)    Coating layers (11a,11b)
NOVELTY - Composite type oxygen-free decayed ecological natural fertilizer, comprises 20-40 wt.% liquid manure, 20-40 wt.% dung and 30-50 wt.% weed leaves.    USE - As composite type oxygen-free decayed ecological natural fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the ecological natural fertilizer, which involves weighing the above-mentioned raw material, placing in a manure pit covered with environment-friendly plastic film, and adding 400-600 g synthetic liquid for performing enzymolysis, uniformly mixing, and sealing the pit until fermentation is completed.
NOVELTY - Method for preparing grain organic fertilizer using waste tobacco stalk involves crushing waste tobacco stalk and vinasse as organic fertilizer raw material, and adding fresh chicken manure, adding fermentation microbial inoculum to the mixture, performing stacking fermentation at normal temperature of 70 degrees C for 15-25 days, where the water content of the fermented mixture is less than 25%, and decomposing the fermented material to obtain powdered or granular refined organic fertilizer.    USE - The method is useful for preparing grain organic fertilizer using waste tobacco stalk (claimed).    ADVANTAGE - The method enables to prepare product within short period of time and which causes less odor during fermentation process.    DETAILED DESCRIPTION - Method for preparing grain organic fertilizer using waste tobacco stalk involves crushing waste tobacco stalk and vinasse as organic fertilizer raw material with granularity of less than 2 mm, and adding fresh chicken manure in a mass ratio of 7:3, uniformly mixing the mixture, and adding fermentation microbial inoculum in a mass ratio of 10:1, where the microbial fermentation microbial inoculum includes Lactobacillus acidophilus, fish ferment bacteria and JS8 chicken manure proteolytic strains in a ratio of 2-3:1-2:3-4, performing stacking fermentation at normal temperature of 70 degrees C for 15-25 days, where the water content of the fermented mixture is less than 25%, and decomposing the fermented material to obtain powdered or granular refined organic fertilizer.
NOVELTY - Functional nutritional agent comprises 5-8 wt.% urea, 13-22 wt.% phosphoric acid, 3-7 wt.% sodium carbonate, 2-7 wt.% ammonium sulfate, 1-5 wt.% iron EDTA, 0.5-3 wt.% zinc-N-2-hydroxyethyl-ethylenediaminetriacetate, 0.5-3 wt.% manganese EDTA, and 50-70 wt.% weathered lignite leaching liquor.    USE - The functional nutritional agent is useful for repairing and restoring plant (claimed), promoting plant root system to grow and fruits, preventing injury caused by climate, fertilizer and pests.    ADVANTAGE - The agent rapidly restores vitality, increases crop yields, improves yield of crop, required in reduced dosage, and is convenient to use, environmentally-friendly, less labor-intensive, and prepared simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the functional nutritional agent, which involves immersing weathered coal in water for 20-25 days, maintaining dissolved oxygen content in water to 1.5-2.5 mg/l, taking the oxygen-enriched liquid, adding weathered coal, stirring and reacting for 80-120 days, taking the reaction liquid while stirring adding pH regulator, adjusting the pH to 5-7, standing, precipitating the reaction liquid to obtain weathered lignite leaching liquor, adding the remaining above-mentioned raw materials and mixing to obtain product.
NOVELTY - Flower nutritional soil comprises raw materials comprising 30-35 pts. wt. humus, 25-30 pts. wt. garden soil, 25-30 pts. wt. river sand, 10-15 pts. wt. activated sludge, 5-10 pts. wt. bone meal, 10-15 pts. wt. rotten farmyard manure, 10-15 pts. wt. sawdust and 2-5 pts. wt. microorganism.    USE - As flower nutritional soil.    ADVANTAGE - The nutritional soil has short fermenting time and good soil ventilation property, and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the nutritional soil, which involves mixing the above-mentioned raw materials, fermenting the mixture for 4-5 days, stirring the mixture once for every 8-10 hours, drying, crushing and sieving to obtain soil.
NOVELTY - Flammulina velutipes planting material comprises sawdust, wheat bran, gypsum powder, lime powder, magnetite powder, bentonite, Lactobacillus, rice bran, soybean meal, Citrus slag, buckwheat hull, Lavender, Cassia seed, silkworm excrement, nutritional additives and soy milk. The nutrient additives include vitamin C, wheat gluten protein, Angelica oil, barley oil, zinc chloride, cypress wine, affine cudweed and quisqualis and are obtained by dissolving vitamin C in water for to obtain vitamin C solution, and crushing affine cudweed and quisqualis.    USE - Flammulina velutipes planting material.    ADVANTAGE - The Flammulina velutipes planting material can be easily and economically prepared with rich nutritional value, delicious taste and high yield and quality, and ensures the rapid growth of mycelium.    DETAILED DESCRIPTION - Flammulina velutipes planting material comprises 40-45 pts. wt. of sawdust, 30-35 pts. wt. of wheat bran, 1-1.5 pts. wt. of gypsum powder, 1-2 pts. wt. of lime powder, 3-4 pts. wt. of magnetite powder, 9-10 pts. wt. of bentonite, 0.2-0.3 pts. wt. of Lactobacillus, 20-22 pts. wt. of rice bran, 10-12 pts. wt. of soybean meal, 7-8 pts. wt. of Citrus slag, 10-12 pts. wt. of buckwheat hull, 2-3 pts. wt. of Lavender, 1.5-2 pts. wt. of Cassia seed, 2-2.5 pts. wt. of silkworm excrement, 4-5 pts. wt. of nutritional additives and 20-22 pts. wt. of soy milk. The nutrient additives include 0.2-0.3 pts. wt. of vitamin C, 0.2-0.3 pts. wt. of wheat gluten protein, 0.03-0.05 pts. wt. of Angelica oil, 0.03-0.04 pts. wt. of barley oil, 0.05-0.07 pts. wt. of zinc chloride, 10-12 pts. wt. of cypress wine, 2-3 pts. wt. of affine cudweed and 1-2 pts. wt. of quisqualis and are obtained by dissolving vitamin C in water for 10-12 times to obtain vitamin C solution, crushing affine cudweed and quisqualis, mixing with adding cypress wine, adding vitamin C solution to the material, drying and mixing with remaining material.
NOVELTY - Bio-organic fertilizer comprises 150-650 pts. wt. of active organic fertilizer, 200-450 pts. wt. of inorganic fertilizer, 20-200 pts. wt. of tanarius, 30-150 pts. wt. of peat soil, 10-100 pts. wt. of Cassava residue, and 50-350 pts. wt. of wheat bran. The active organic fertilizer comprises 10-50 pts. wt. of actinomycete bacteria powder, 15-40 pts. wt. of spore Bacillus cereus powder, 25-60 pts. wt. of Rhizobium sinensis, and 10-35 pts. wt. of Cordyceps sinensis.    USE - The bio-organic fertilizer is useful for inhibiting soil-borne disease.    ADVANTAGE - The efficient and diversified bio-organic fertilizer has no pollution and public hazard, improves soil structure at middle and low producing field, drought resistance, and low preparation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bio-organic fertilizer comprising adding and mixing actinomycete bacteria powder, spore Bacillus cereus powder, Rhizobium sinensis, and Cordyceps sinensis, maintaining the mixture at 70-85 degrees C, then fermenting for 5-10 days to obtain active organic bacteria microbial inoculum, adding inorganic fertilizer, tanarius, peat soil, and Cassava residue and uniformly mixing to obtain microorganism material, adding active organic fertilizer and wheat bran, uniformly mixing, peleting and drying at 120-180 degrees C , crushing, and then screening.
NOVELTY - Fertilizer comprises urea, potassium mineral powder, phosphorite powder, grass carbon, edible fungi bran, zinc sulfate heptahydrate, magnesium sulfate heptahydrate, potassium chloride, calcium superphosphate, calcium magnesium phosphate fertilizer, modified clay powder, brown sugar, vermiculite, shell powder, radish leaf powder, tuckahoe,Pyrethrum, mulberry leaf, poplar tree leaf, and vitamin C.    USE - The fertilizer is useful for camphor tree.    ADVANTAGE - The fertilizer reduces the frequency of fertilizer, improves the soil quality, and improves the quality and disease resistance and insect resistance of the trees.    DETAILED DESCRIPTION - Fertilizer comprises 23-25 pts. wt. of urea, 11-13 pts. wt. of potassium mineral powder, 8-10 pts. wt. of phosphorite powder, 10-12 pts. wt. of grass carbon, 3-5 pts. wt. of edible fungi bran, 2-4 pts. wt. of zinc sulfate heptahydrate, 4-6 pts. wt. of magnesium sulfate heptahydrate, 6-8 pts. wt. of potassium chloride, 7-8 pts. wt. of calcium superphosphate, 1-2 pts. wt. of calcium magnesium phosphate fertilizer, 10-12 pts. wt. of modified clay powder, 1-2 pts. wt. of brown sugar, 18-22 pts. wt. of vermiculite, 3-5 pts. wt. of shell powder, 1-2 pts. wt. of radish leaf powder, 1-2 pts. wt. of tuckahoe, 2-4 pts. wt. of Pyrethrum, 1-2 pts. wt. of mulberry leaf, 1-2 pts. wt. of poplar tree leaf, and 0.2-0.4 pts. wt. of vitamin C.
NOVELTY - Preparation of granular superphosphate comprises reacting phosphorus ore slurry and sulfuric acid at 50-110 degrees C for 1-5 hours, stirring and drying.    USE - Method for preparing granular superphosphate (claimed).    ADVANTAGE - The method is energy-saving, environmental-friendly and useful.
NOVELTY - Comprehensive utilization of magnesium-smelting furnace slag comprises crushing magnesium-smelting furnace slag; dissolving crushed slag in acid; filtering; adding filtrate with precipitating agent to obtain calcium chloride calcium sulfate dihydrate precipitate; and performing secondary filtering to obtain calcium sulfate dihydrate precipitate in form of gypsum powder and secondary filtrate as liquid fertilizer.    USE - Comprehensive utilization of magnesium-smelting furnace slag.    ADVANTAGE - The method effectively uses magnesium-smelting furnace slag waste, thus effectively minimizing environment pollution.
NOVELTY - Fertilizer comprises nitrogen-phosphorus-potassium fertilizer, biogas residue, egg shell powder, rapeseed cake, weathered coal, bamboo charcoal, furfural dreg, stone powder, neatsfoot oil, germanium oxide, boron, ferrous sulfate, manganese sulfate, ammonium sulfate, copper sulfate, humic acid, dyer's wood leaf, broad bean shell, grass, cat claw, and Chinese Bupleurum root.    USE - The fertilizer is useful for mulberry.    ADVANTAGE - The fertilizer reduces the frequency of fertilizer, improves the soil quality, and improves the quality and disease resistance and insect resistance of the trees.    DETAILED DESCRIPTION - Fertilizer comprises 24-28 pts. wt. of nitrogen-phosphorus-potassium fertilizer, 17-19 pts. wt. of biogas residue, 10-12 pts. wt. of egg shell powder, 9-11 pts. wt. of rapeseed cake, 20-25 pts. wt. of weathered coal, 8-10 pts. wt. of bamboo charcoal, 4-6 pts. wt. of furfural dreg, 2-4 pts. wt. of stone powder, 4-6 pts. wt. of neatsfoot oil, 1-3 pts. wt. of germanium oxide, 0.5-1.0 pts. wt. of boron, 1-2 pts. wt. of ferrous sulfate, 1-2 pts. wt. of manganese sulfate, 3-5 pts. wt. of ammonium sulfate, 2-4 pts. wt. of copper sulfate, 4-6 pts. wt. of humic acid, 1-2 pts. wt. of dyer's wood leaf, 10-15 pts. wt. of broad bean shell, 2-4 pts. wt. of grass, 1-2 pts. wt. of cat claw, and 1-2 pts. wt. of Chinese Bupleurum root. An INDEPENDENT CLAIM is included for preparing the fertilizer comprising weighing each raw material, uniformly mixing and crushing, and then adding 0.1-0.3% of effective microorganisms (EM), uniformly mixing then fermenting for 10-15 days, then adding water, granulating, and drying.
NOVELTY - A bean seed is treated by doing plasma treatment on bean seed, using special drought-resisting coating agent.    USE - Treatment of bean seed for preventing drought (claimed).    ADVANTAGE - Method effectively promotes seed germination, increases drought resistance and culturing seedling, and is environment-friendly.
NOVELTY - Preparation of 7-(4-chloro/bromobutoxy)-3,4-dihydrocarbostyril compound (II), comprises reacting hydroxy-3,4-dihydro-2(1H)-quinolinone compound (III) with 1-bromo-4-chlorobutane using super base in presence of water and a phase transfer catalyst.    USE - (II) is useful as a key intermediate for the preparation of aripiprazole, which is useful for treating schizophrenia.    ADVANTAGE - The process provides (II) with high purity ( greater than or equal to 97.5% determined by HPLC) and less content of dimmer impurity ( less than or equal to 1% determined by HPLC) in an eco- friendly, cost-effective and industrial scalable manner.    DETAILED DESCRIPTION - Preparation of 7-(4-chloro/bromobutoxy)-3,4-dihydrocarbostyril compound of formula (II), comprises reacting hydroxy-3,4-dihydro-2(1H)-quinolinone compound of formula (III) with 1-bromo-4-chlorobutane using super base in presence of water and a phase transfer catalyst.    X = Cl or Br.
NOVELTY - Preparation of Montelukast involves: reacting 2-(2-(3(S)-(3-(2-(7-chloro-2-quinolinyl)-ethenyl)phenyl)-3-methanesulfonylpropyl) phenyl)-2-propanol with 1-(mercaptomethyl) cyclopropane acetic acid in presence of sodium alkoxide and solvent such as N-methyl 2-pyrrolidone.    USE - For preparation of montelukast (claimed) as an anti-asthmatic, anti-allergic, anti-inflammatory and cytoprotective agent.    ADVANTAGE - The method is improved, simple, cost-effective and environment friendly process for the preparation of Montelukast and its amine salts.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) purification of Montelukast isopropylamine salt involving: providing Montelukast in mixture of isopropyl alcohol and toluene; adding isopropylamine, and isolating Montelukast isopropylamine salt free of sulfoxide impurity; and    (2) purification of Montelukast involving: dissolving Montelukast isopropylamine in a mixture of water and water immiscible organic solvent; adjusting pH to acidic; adding alcoholic sodium hydroxide solution; passing the reaction mass through Silica gel and isolating Montelukast free of impurities D and E.
NOVELTY - Bed comprises a structure or cover made of woven or nonwoven materials i.e. 100% pure polyester, cotton or polyamide, which is treated with neem essential oils, andiroba oil and citronella oil in microencapsulated and nanocoated form. The oil material is applied by industrial impregnation of fibers or non-woven fabric in concentration of 0.3-1.5%, preferably 0.77%.    USE - Bed for domestic animals for repelling insects, particularly fleas and ticks (claimed).    ADVANTAGE - The bed is eco-friendly and has long shelf-life.
NOVELTY - Fuel comprises 90-95% of denatured ethanol and an inorganic compound including strontium, boron, copper, potassium, calcium or iron.    USE - Fuel for generating entertainment shows flames of different colors.    ADVANTAGE - The fuel minimizes generation of fumes and splashing, and provides conventional fire and flames with high safety and security.
NOVELTY - The device comprises a pumping unit including chamber designed to house inside a piston connected to a hydraulic drive equipment, and a feed line (1) for supplying biomass to a mixing chamber coincides with the pumping equipment. A valve unit is provided for controlling flow of process water from a tank for storage of processing water, where a cylinder is located in the mixing tank. A locking device is designed in conduit for connecting the cylinder to the reactor. The cylinder located below the mixing vessel comprises a series of holes located along its surface.    USE - Device for controlling ratio of process water and biomass in hydrothermal carbonization process.    ADVANTAGE - The device comprises a pumping unit including chamber designed to house inside a piston connected to a hydraulic drive equipment, and thus the piston can move enough and forms a seal against pressure process, and prevents abrasive streams.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling ratio of process water and biomass in hydrothermal carbonization process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for controlling ratio of process water and biomass in hydrothermal carbonization process.    Feed line (1)    Mixing vessel (2)    Hydraulic pump cylinder (4)    Hydraulic oil (5)    Gate valve (9)
NOVELTY - High-efficient organic fertilizer comprises 14-27 pts. wt. pig manure, 13-18 pts. wt. pond sludge, 14-17 pts. wt. maize straw, 2-8 pts. wt. attapulgite, 3-12 pts. wt. humic acid, 3-9 pts. wt. oil shale, 3-9 pts. wt. rock phosphate powder, 0.3-0.9 pts. wt. radix sophorae flavescentis, and 0.7-1.3 pts. wt. biological bacteria.    USE - As high-efficient organic fertilizer.    ADVANTAGE - The fertilizer reduces insect-pest of crops, is easy to control and rich in organic matter, nitrogen, phosphorus, potassium and various microelements, provides long-lasting effect, improves soil structure, increases crop yield and production that can reach more than 15%, and can be prepared simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves (a) weighing and heating the pig manure and pond sludge using heating chamber at 105-120 degrees C for 30-50 minutes, (b) cooling the product obtained in the step (a) to room temperature, adding the cooled product in mixer, then adding maize straw, attapulgite, humic acid and biological bacteria to the mixer, uniformly mixing the mixture, and performing fermentation at 38-48 degrees C for 24-48 hours, and (c) adding oil shale, rock phosphate powder and radix sophorae flavescentis to the fermented product, and uniformly mixing the mixture to obtain organic fertilizer.
NOVELTY - Organic fertilizer and method for preparing organic fertilizer are claimed. The organic fertilizer comprises 14-19 pts. wt. animal bone powder, 17-21 pts. wt. rabbit manure, 13-17 pts. wt. cow dung, 12-17 pts. wt. furfural residue, 13-21 pts. wt. soybean meal, 3-6 pts. wt. gypsum powder, 7-13 pts. wt. potassium powder, 0.6-1.1 pts. wt. fermenting agent, and 3-7 pts. wt. sugar.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer improves soil structure and increases crop yield, and is highly effective for a long period of time.    DETAILED DESCRIPTION - Organic fertilizer and method for preparing organic fertilizer are claimed. The organic fertilizer comprises 14-19 pts. wt. animal bone powder, 17-21 pts. wt. rabbit manure, 13-17 pts. wt. cow dung, 12-17 pts. wt. furfural residue, 13-21 pts. wt. soybean meal, 3-6 pts. wt. gypsum powder, 7-13 pts. wt. potassium powder, 0.6-1.1 pts. wt. fermenting agent, and 3-7 pts. wt. sugar. The method involves (a) heating the above-mentioned animal bone powder, rabbit manure, furfural residue, soybean meal, and cow dung at 60-80 degrees C for 20-40 minutes and cooling to room temperature, (b) adding the heated material to fermentation chamber and adding the above-mentioned fermenting agent and sugar to the chamber, and sealing the chamber, where fermentation is carried over at 35-45 degrees C for 36-48 hours, and (c) adding the above-mentioned gypsum powder and potassium powder to the obtained fermented product, and uniformly stirring the product.
NOVELTY - A fertilizer comprises rabbit dung, lees, glutinous rice roots, yeast plant waste, turpentine, potassium chloride, urea, talcum powder, ammonium chloride, white granulated sugar, sodium lignosulfonate, nanojade powder, ferrous sulfate, sodium metasilicate, zinc chloride, polyvinyl alcohol, propanediol, Viola, Sphaerobolus, Wisteria flowers and orange blossom.    USE - Fertilizer used for Chinese gooseberry.    ADVANTAGE - The fertilizer reduces insect pests and plant diseases, reduces fertilizing time, and improves soil quality yield of Chinese gooseberry.    DETAILED DESCRIPTION - A fertilizer comprises 23-28 pts. wt. rabbit dung, 17-19 pts. wt. lees, 10-12 pts. wt. glutinous rice roots, 5-6 pts. wt. yeast plant waste, 2-4 pts. wt. turpentine, 5-7 pts. wt. potassium chloride, 3-5 pts. wt. urea, 18-22 pts. wt. talcum powder, 1-2 pts. wt. ammonium chloride, 5-8 pts. wt. white granulated sugar, 2-3 pts. wt. sodium lignosulfonate, 4-6 pts. wt. nanojade powder, 1-3 pts. wt. ferrous sulfate, 1-2 pts. wt. sodium metasilicate, 2-4 pts. wt. zinc chloride, 5-7 pts. wt. polyvinyl alcohol, 2-4 pts. wt. propanediol, 1-2 pts. wt. Viola, 1-2 pts. wt. Sphaerobolus, 3-5 pts. wt. Wisteria flowers and 4-6 pts. wt. orange blossom. An INDEPENDENT CLAIM is included for preparation of fertilizer comprising mixing raw materials, crushing, milling, stirring for 2 hours, sealing for 15-20 days at 25-40 degrees C, stirring, stacking, and sealing for 5-10 days.
NOVELTY - Composite microorganism fertilizer, comprises nitrogen-phosphorus-potassium compound fertilizer, composite bacterial liquid and fine rice bran, grass or livestock manure, zeolite powder and humic acid.    USE - The composite microbial fertilizer is useful for improving wheat yield per unit area, controlling occurrence of scab or rust (all claimed), providing bacterial resistance and lodging resistance, and improving and activating soil.    ADVANTAGE - The fertilizer is highly complementary, enables high yield with improved quality, reduces the pesticide residue, and exhibits improved storability.
NOVELTY - Vegetable organic fertilizer comprises 32-47 pts. wt. tree leaf of plant straw, 28-35 pts. wt. human or animal urine and excrement, 22-31 pts. wt. green manure, 12-17 pts. wt. humic acid fertilizer, 8-13 pts. wt. sugar, 0.5-1.2 pts. wt. fermenting agent, and 2.3-4.3 pts. wt. soil modifying agent.    USE - As vegetable organic fertilizer.    ADVANTAGE - The vegetable organic fertilizer improves fertility and water storage ability of the soil, promotes decomposition of organic matter, improves vegetable quality, improves nutrient content of the vegetable, and effectively reduces disease rate of vegetables.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer, which involves (a) weighing and mixing plant straw, human or animal urine and excrement, green manure, and humic acid fertilizer and vacuum heating the mixture in heating chamber at 105-120 degrees C for 20-40 minutes, (b) weighing sugar, fermenting the sugar in fermentation tank, adding the mixture obtained in step (a) to fermentation tank, uniformly stirring the mixture and fermenting the mixture at 45-65 degrees C for 3-5 hours, and (c) mixing the obtained mixture in step (b) and green manure and soil, uniformly stirring the mixture and continuously fermenting the mixture at 40-45 degrees C for 2 hours.
NOVELTY - Sustained-release fertilizer comprises urea, borax, boric acid, manganese sulfate, ammonium citrate, sodium sulfate, calcium carbonate, kaolin, actinolite powder, sodium sulfite, brown sugar, Anemone hupehensis, half leaves of Passiflora plants, swamp mahogany leaves, Sophora root, Glyptostrobus pensilis, Phyla nodiflora, Toddalia, and root of Viburnum lentago.    USE - The sustained-release fertilizer is useful for controlling insects and pests in crops.    ADVANTAGE - The sustained-release fertilizer controls release of urea content, and prevents soil pollution.    DETAILED DESCRIPTION - Sustained-release fertilizer comprises 30-35 pts. wt. urea, 20-25 pts. wt. borax, 5-6 pts. wt. boric acid, 2-4 pts. wt. manganese sulfate, 1-2 pts. wt. ammonium citrate, 1-2 pts. wt. sodium sulfate, 15-20 pts. wt. calcium carbonate, 8-12 pts. wt. kaolin, 7-8 pts. wt. actinolite powder, 2-3 pts. wt. sodium sulfite, 10-12 pts. wt. brown sugar, 2-3 pts. wt. Anemone hupehensis, 1-3 pts. wt. half leaves of Passiflora plants, 8-10 pts. wt. swamp mahogany leaves, 7-8 pts. wt. Sophora root, 3-4 pts. wt. Glyptostrobus pensilis, 1-2 pts. wt. Phyla nodiflora, 1-2 pts. wt. Toddalia, and 1-2 pts. wt. root of Viburnum lentago. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned sustained-release fertilizer, which involves (a) crushing the A.hupehensis, half leaves of Passiflora plants, swamp mahogany leaves, Sophora root, G.pensilis, P.nodiflora, Toddalia and root of V.lentago, uniformly crushing the mixture, adding 0.1-0.3% microbial inoculum comprising essential microorganism, uniformly blending the mixture, adding water and sugar to the mixture and fermenting the mixture for 10-15 days, and (b) weighing urea, heating and melting the urea, granulating the fermented mixture, stirring the granules for 20-30 minutes and drying the granules.
NOVELTY - Method of preparing polycyclic aromatic hydrocarbon polluted soil compost conditioning agent, involves obtaining agricultural production waste mushroom bran of edible mushroom as carrier, soaking the carrier, inoculating culture capable of effectively degrading polycyclic aromatic hydrocarbon mixed solution, mixing uniformly and multiplying the culture at 25-28 degrees C for 24-36 hours to obtain polycyclic aromatic hydrocarbon polluted soil compost conditioning agent.    USE - The method is useful for preparing polycyclic aromatic hydrocarbon polluted soil compost conditioning agent (claimed).    ADVANTAGE - The method improves soil fertility and quality, and is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Method of preparing polycyclic aromatic hydrocarbon polluted soil compost conditioning agent, involves obtaining agricultural production waste mushroom bran of edible mushroom as carrier, soaking the carrier, inoculating culture capable of effectively degrading polycyclic aromatic hydrocarbon mixed solution, mixing uniformly and multiplying the culture at 25-28 degrees C for 24-36 hours to obtain polycyclic aromatic hydrocarbon polluted soil compost conditioning agent, where the edible fungi is Pleurotus eryngii or oyster mushroom, the culture is high-efficiency transposon system pBTn for Gram-positive bacterium, and the polycyclic aromatic hydrocarbon is extracted from coke gas plant.
NOVELTY - Selenium fertilizer comprises 400-500 pts. wt. chicken and duck manure mixture, 30-50 pts. wt. food residue, 80-120 pts. wt. gramineous straw, 50-80 pts. wt. corn cob with corn kernels, 40-60 pts. wt. bentonite, 10-30 pts. wt. radix scutellariae powder and 80-120 pts. wt. purple sweet potato. The mass ratio of chicken manure and duck manure in chicken and duck manure mixture is 3:1.    USE - The selenium fertilizer is useful for improving depleted selenium content in soil (claimed).    ADVANTAGE - The selenium fertilizer: has high amount of organic selenium; significantly improves the absorption rate of the crop; and increases selenium content in crops by 35% and in food products by 18-22%.
NOVELTY - Organic cultivation substrate comprises 20-30 pts. vol. coconut husk, 15-25 pts. vol. carbon powder and 30-40 pts. vol. black fungus mushroom residue.    USE - The substrate is useful: in the cultivation of vegetables in uncultivated lands and potted plants; and for improving the soil environment, and soil fertility.    ADVANTAGE - The substrate provides abundant and comprehensive nutrition elements to the plants; completely utilizes the waste as raw material produced in the agricultural production; and is environmental friendly, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the substrate, comprising (i) adjusting the carbon to nitrogen ratio of black fungus mushroom residue to 25-30:1, adding aerobic fermentation bacteria, windrow or pile of fermentation product, allowing the fermentation product to become brown uniformly, bulk amount and dry, where the carbon to nitrogen ratio in the fermentation product is 15-17:1, to obtain mushroom residue fermentation product; (ii) washing the mixture with salt, adding coconut husk and mushroom residue fermentation product, mixing, and spraying antagonistic bacteria, and aging windrow or pile of fermentation product for 20-40 days, until the water content is 20-30% to obtain a bio-based material; and (iii) mixing the bio-base material with carbon powder to obtain the product.
NOVELTY - Biologically active substrate product comprises a common seedling substrate added with functional strain Bacillus amyloliquefaciens SQR9 (CGMCC NO.5808).    USE - The biologically active substrate product is useful for cucumber seedling (claimed) in promoting growth, improving crops yield and preventing and controlling cucumber soil-borne diseases.
NOVELTY - Method for producing biological fertilizer, involves performing high density liquid fermentation using Bacillus subtilis, Pseudomonas aeromonas, Lactobacillus plantarum and B.thuringiensis, obtaining concentrated microbial inoculum, mixing 30-100 pts. wt. microbial inoculum, 100-300 pts. wt. decomposed straw powder, 100-150 pts. wt. urea, 50-120 pts. wt. potassium chloride, and 80-150 pts. wt. diatomite, placing in granulator for granulating, taking the pelleting material, drying, and placing in cylinder to obtain product.    USE - The method is useful for producing the biological fertilizer which is useful in planting crops (all claimed).    ADVANTAGE - The method is simple and cost-effective to perform, and is suitable for the industrial production.    DETAILED DESCRIPTION - Method for producing biological fertilizer, involves performing high density liquid fermentation using Bacillus subtilis, Pseudomonas aeromonas, Lactobacillus plantarum and B.thuringiensis, after performing fermentation obtaining concentrated microbial inoculum with the spore content up to 1011-1012 colony forming unit (cfu)/g, where the viable count of Bacillus subtilis is 109-1010 cfu/g, Pseudomonas aeromonas is 107-108 cfu/g, Lactobacillus plantarum is 108-109 cfu/g and B.thuringiensis is 107-108 cfu/g, weighing 30-100 pts. wt. microbial inoculum, 100-300 pts. wt. decomposed straw powder, 100-150 pts. wt. urea, 50-120 pts. wt. potassium chloride, and 80-150 pts. wt. diatomite, mixing uniformly, placing in extrusion granulator for granulating, taking the pelleting material and drying, placing the dried granules in a cylinder to obtain product.
NOVELTY - Cultivating material of Pleurotus mushroom, comprises 50-60 wt.% sugarcane waste, 20-30 wt.% corn cob, 15 wt.% rice bran, 2 wt.% lime powder, 1 wt.% urea, 1 wt.% calcium superphosphate and 1 wt.% gypsum powder.    USE - Cultivating material of Pleurotus mushroom.    ADVANTAGE - The cultivating material can be easily absorbed by the mycelium as it contains simple substance, promotes the growth and yield of P.matsuchi mushroom, and has biological efficiency of 98.3-115.2%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing cultivating material of Pleurotus mushroom, which involves soaking the sugarcane chips in lime water, directly piling the materials, adding urea followed by water, naturally fermenting the materials for 16-18 days, adding gypsum powder and calcium superphosphate, corn cob and rice bran, adding water, stopping fermentation, maintaining the water content of the culture material at 63-65%, packaging the product in a polypropylene plastic bag, each bag containing wet material of 1100-1200 g, sterilizing at 100 degrees C and cooling the material to less than 25 degrees C.
NOVELTY - Sulfonated humic acid product, obtained by dissolving gaseous, liquid or solid state sulfur trioxide in aprotic solvent to obtain sulfur trioxide solution, reacting sulfur trioxide solution with humic acid at suitable reaction temperature, separating and washing, is claimed.    USE - The sulfonated humic acid product is useful: as cement water reducing agent, drilling fluid additive and water-coal-slurry additive; for producing surfactant, water-retaining agent, sustained and controlled release bio-material material and fertilizer (all claimed). The acid product is useful as acid fertilizer for acid-resistance rice and other crops and as biological culture medium composition (all claimed).    ADVANTAGE - The method: easily separates and recovers sulfur trioxide (claimed); is simple and economical; has mild reaction conditions; provides high purity products; reduces production cost and is environmentally friendly.
NOVELTY - Preparing liquid fertilizer comprises extracting Stevia to obtain extract, introducing micro organism into the extract, and fermenting the extract.    USE - The method is useful for preparing liquid fertilizer (claimed).    ADVANTAGE - The method is capable of preparing the liquid fertilizer in an eco-friendly manner.
NOVELTY - Compost composition comprises 65-75 pts. wt. animal waste, 12-18 pts. wt. washed coal bottom ash, 12-18 pts. wt. pulverized perlite, 1-3 pts. wt. pulverized gypsum, based on 100 pts. wt. compost composition.    USE - The compost composition is useful for cultivating crops, preferably lettuce (all claimed).    ADVANTAGE - The compost composition is produced in cost-efficient manner, improves soil physical properties and soil air permeability, can be composted in rapid manner, prevents the loss of organic carbon and nitrogen compounds, and slowly diffuses into soil and thus it serves as sustained release carrier.    DETAILED DESCRIPTION - INDEPENDENT CLAIM are also included for    (1) preparing compost composition, comprising (a) mixing animal waste, washed coal bottom ash, pulverized perlite and pulverized gypsum to prepare a mixture, and (b) composting the prepared mixture at 50-60 degrees C; and    (2) cultivating crops by applying the compost composition in crops field
NOVELTY - Bacillus subtilis JS strain preserved under a preservation number of KCTC 12264BP, is new.    USE - The Bacillus subtilis JS strain is useful in a bio-fertilizer for promoting the aerial part and root growth of a plant such as tobacco, lettuce or Ipomoea batatas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a microbe form for plant growth promotion including the strain or its culture fluid as an active ingredient;    (2) manufacturing a bio-fertilizer comprising cultivating the strain; and    (3) promoting the outgrowth of the plant including dipping a seed of the plant in the strain.
NOVELTY - Sterilization module comprises a substrate electrically connected to the sterilization module having metal lath type electrode, where the metal lath has a mesh of rhombus shape with longitudinal width (LW) of 4.4 plus minus 0.3 mm and narrow width (SW) of 26 plus minus 0.3 mm.    USE - Used as a sterilization module having metal lath type electrode.    ADVANTAGE - The sterilization module: reduces the prevention of electrode reduction phenomenon due to generation of hydrogen gas, thus improving the product performance; comprises electric wire connected to the center of the lower cover, thus saving large amount of space for sterilization; reduces the power consumption; and comprises water-proof membrane, which occupies less space. The cleaner with sterilized water: comprises electric wire, which is adhered to the side of the cleaner with sterilized water and inclined sideward, thus reducing the resistance of water, reducing power consumption, maintains the sterilized water to remain inside the cleaner and maintains hygienic conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a cleaner with sterilized water comprising the sterilization module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the metal lath type electrode of the sterilization module.    Cathode (65)    Anode (66)
NOVELTY - An environment-friendly energy-saving type one marsh gas pool stirrer. It comprises a fan, a thrust ball bearing base, a radial bearing base, a transmission shaft and stirring frame, thrust ball bearing base is installed on the biogas tank cover surface, the inner part is provided with a thrust ball bearing, centripetal bearing base is installed on the upper end of air outlet hole of the marsh gas tank, the inner part is equipped with radial bearing, a fan and stirring frame are respectively installed on the upper's lower end of transmission shaft. The utility model has the following beneficial effects: using natural wind as the power source, not only saves energy and is good for environmental protection, and it does not need manual stirring, so it will not cause gas leakage and personal injury. The structure design is reasonable and simple, and the cost is low. Can not stop the scum layer taking marsh gas tank, the biogas generated successfully overflow fermentation material liquid, so as to greatly improve's gas production rate.
NOVELTY - An intelligent automatic high-one integrated marsh gas tank system, comprising a biogas tank, a temperature control device, a pressure control device, control device, slag processing device and programmable controller, marsh gas tank is cylindrical hydraulic marsh gas tank, one side is provided with a feeding port, and the other side is connected with the water tank, the upper end is provided with an air supply hole, a temperature control device, a pressure control device, control device, slag processing device and programmable controller is mounted on the internal or external's marsh gas tank, and the temperature control device, the pressure control device, control device and biogas residue processing device is connected with the programmable controller; The utility model claims an intelligent automatic high-integrated marsh gas tank's system has the following beneficial effects: (1), the intelligent automatic, (2) high integration, (3) modular, (4); (5) operation is simple, the maintenance is convenient, and the cost is low.
NOVELTY - Organic fertilizer comprises 40-50 pts. wt. of fresh cow dung, 30-40 pts. wt. of rice husk powder, 25-30 pts. wt. of straw, 1-3 pts. wt. of microorganism, 7-12 pts. wt. of zeolite, 8-11 pts. wt. of tea leaves, 10-13 pts. wt. of soil improvers, 2-3 pts. wt. of zinc sulfate, 2-4 pts. wt. of iron sulfate, 1-2 pts. wt. of copper sulfate, and 1-2 pts. wt. of manganese sulfate.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer can effectively improve the soil physicochemical property and soil nutritional value, and promotes the growth of the crops.    DETAILED DESCRIPTION - Organic fertilizer comprises 40-50 pts. wt. of fresh cow dung, 30-40 pts. wt. of rice husk powder, 25-30 pts. wt. of straw, 1-3 pts. wt. of microorganism, 7-12 pts. wt. of zeolite, 8-11 pts. wt. of tea leaves, 10-13 pts. wt. of soil improvers, 2-3 pts. wt. of zinc sulfate, 2-4 pts. wt. of iron sulfate, 1-2 pts. wt. of copper sulfate, and 1-2 pts. wt. of manganese sulfate. The soil improver comprises 100-120 pts. wt. of diatomite, 1-2 pts. wt. of nano toner, 4-5 pts. wt. of neatsfoot oil, 4-5 pts. wt. of sodium metasilicate, 1-2 pts. wt. of silane coupling agent, 3-4 pts. wt. of sodium selenite, 2-3 pts. wt. of chitosan, 1-2 pts. wt. of eucalyptus oil, 1-2 pts. wt. of alcohol esters, 2-3 pts. wt. of nano powder, 4-5 pts. wt. of Alangium root, 3-4 pts. wt. of garlic, and water, where the organic fertilizer is prepared by: adding Alangium root and diatomite with water; crushing the garlic into powder; then heating the above materials at a temperature of 80-90 degrees C; adding nano powder and nano toner and then continuously grinding for 30-45 minutes; finally adding sodium silicate and chitosan and stirring into a paste for 10-15 minutes, then adding other remaining ingredients; and drying the material to obtain a product.
NOVELTY - A methanol gasoline with high mutual solvent contains 85 wt.% gasoline, 12 wt.% methanol, and 3 wt.% composite additive.    USE - A methanol gasoline with high mutual solvent (claimed).    ADVANTAGE - Flow rate ratio is constant, and product quality is high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pipeline processing of methanol gasoline with high mutual solvent which involves preparing gasoline, methanol, and composite additive by batch controller operation panel or upper position machine, distributing oil to 3 system, subjecting used oil in instantaneous line process of methanol, calculating gasoline and additive instantaneous pipeline capacity, sending system instruction to start pipeline pump and electro-hydraulic valve, starting gasoline, methanol and composite additive for 10 s, starting system according to 3 oil quantity with given electro-hydraulic valve initial opening degree, accelerating electro-hydraulic valve for 14-16 s, measuring system methanol flow rate to 15-25 m3/hour, measuring gasoline flow rate to 80-90 m3/hour, measuring composite additive flow rate to 3-10 m3/hour, transmitting oil, gradually reducing flow speed, decelerating electro-hydraulic valve, gradually reducing opening degree, closing valve oil, reducing dosage in pipeline to ensure no residual methanol and additive, stopping gasoline pump, subjecting through static mixer when testing analysis is finished, subjecting to activated tank, subjecting qualified product to product oil tank, and returning unqualified product to mixing tank.
NOVELTY - An alcohol-based biodiesel contains 2-5 pts. wt. modified alcohol, 2-5 pts. wt. polybasic alcohol, 8-15 pts. wt. bio-oil, 50-65 pts. wt. line oil, 15-20 pts. wt. kerosene, 1-4 pts. wt. cetane value agent, 0.1-0.3 pt. wt. stabilizing agent, and 0.7-0.9 pt. wt. strength agent in which modified alcohol is mixed reactant which consists of methanol, acetone, dimethyl ether, sodium chloride, ferrocene, polyisobutylene, and polyethylene-vinyl acetate, stabilizing agent is oleic acid cyclic acid, diethylamine and/or propylamine, and strength agent is grease, amyl nitrite, and/or tetranitromethane.    USE - An alcohol-based biodiesel (claimed).    ADVANTAGE - Product reduces tail gas emission and hydrocarbon emission and has strong water resistance, raw material is simple and wide, cost is low, storage time is long and not layered, and burning performance is good.
NOVELTY - An alcohol-based clean vehicle fuel comprises 25-45 wt.% aromatic hydrocarbon, 25-69 wt.% naphtha, 5-30 wt.% denatured alcohol, 0.1-0.3 wt.% stabilizer, and 0.7-0.9 wt.% strong fuel agent in which denatured alcohol contains methanol, acetone, isopropanol or isobutanol, dimethyl ether, and sodium chloride, stabilizer is oleic acid, cyclic acid, diethylamine, or propylamine, and strong fuel agent is mixture of isoamyl nitrite and tetranitromethane.    USE - An alcohol-based clean vehicle fuel (claimed).    ADVANTAGE - The vehicle fuel composition is simple, has strong water resistance and good burning performance, is not layered, and does not easily deteriorate, the source of raw material is wide, and production cost is low.
NOVELTY - A food waste biogas desulfurization device comprises purification tank (1) equipped with safety device (3) connected to inlet of biogas tank (5) and connected to gas discharge port of biological desulfurization tower (6) through pipeline, water supply pipe (4) for supplying water to safety device, air supply pump (7), and circulating pump (8). Desulfurization tower is connected to exhaust port.    USE - A food waste biogas desulfurization device (claimed).    ADVANTAGE - The biogas desulfurization device has simple structure and low operating costs, and is safe to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biogas desulfurization device. (Drawing includes non-English language text).    Purification tank (1)    Safety device (3)    Water supply pipe (4)    Biogas tank (5)    Biological desulfurization column (6)    Air supply pump (7)    Circulating pump (8)
NOVELTY - Morpholine salt ionic liquid catalyst (I) is new.    USE - (I) is useful for catalyzing waste oil to produce biodiesel (claimed).    ADVANTAGE - (I): has high catalytic activity within small dosage range, better performance under mild reaction condition, and low toxicity; ensures high product yield; and is easy to degrade, and environment-friendly.    DETAILED DESCRIPTION - Morpholine salt ionic liquid catalyst of formula (I) is new.    R = alkyl.    INDEPENDENT CLAIMS are also included for:    (1) preparation of (I); and    (2) use method of (I) for catalyzing waste oil to produce biodiesel, comprising carrying out esterification and transesterification of waste oil with alcohol in presence of (I).
NOVELTY - Processing glyphosate wastewater, comprises adding glyphosate and aluminum chloride in a beaker, adding 100 ml of distilled water to dissolve, adjusting the pH of solution to be neutral, drying the solution at 30 degrees C for 9 hours, filtering the liquid using a water vacuum pump, adding the filter cake into an electro-thermal constant temperature air blowing drying box for drying, performing nitrosylation to the filtrate using an UV spectrophotometer, performing infrared spectrum detection to the filtrate, and testing a content of organic pollutant.    USE - The method is useful for processing glyphosate wastewater (claimed).    ADVANTAGE - The method is capable of processing glyphosate wastewater with less energy consumption and reduced emission in a simple and eco-friendly manner.    DETAILED DESCRIPTION - Processing glyphosate wastewater, comprises adding 1 g of 95 % of glyphosate and aluminum chloride in a beaker, where the mole ratio of aluminum chloride to glyphosate is 1:4, adding 100 ml of distilled water to dissolve, then adjusting the pH of solution to be neutral by adding sodium hydroxide, drying the solution at 30 degrees C for 9 hours, filtering processing liquid using a water vacuum pump, then adding the filter cake into an electro-thermal constant temperature air blowing drying box for drying, performing nitrosylation to the filtrate using an UV spectrophotometer, performing infrared spectrum detection to the filtrate, and testing content of organic pollutant.
NOVELTY - Using waste of the brewing industry includes carrying out solid-liquid separation of brewing residue to obtain a moisture content of 60% slag; adding 20 wt.% rice bran and 0.1 wt.% enzyme bacteria fast rotting agent, adjusting the pH value to 5.5-7, stirring uniformly, and taking aerobic fermentation; heating and drying the obtained material; crushing; and carrying out granulated molding of the obtained material.    USE - Method for using waste of the brewing industry (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Preparing bio-organic fertilizer manure includes choosing a flat ground without water in the open space, separating 1000 kg chicken manure from the manure pile and additives, and dividing into five equal parts; selecting flat and higher ground; spreading bacteria in the prepared chicken manure, stirring uniformly, and processing the other four stack chicken manure using the same method to deal with another four stack chicken manure; after composting, automatic heating, and fermenting; and drying the fermented material, crushing and sieving to obtained the finished product and packaging.    USE - Method for preparing bio-organic fertilizer manure (claimed) used for improving crop immunity.    ADVANTAGE - The method can improve the quality of crop yield.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer manure comprises:    (A) choosing a flat ground without water in the open space, separating 1000 kg chicken manure from the manure pile and additives, and dividing into five equal parts;    (B) selecting flat and higher ground to avoid the draft, digging parallel ventilation ditch with 30 cm wide trench, 30 cm deep, and 20 cm wide branches from bamboo, spreading straw on the cross beam, and forming a bottom fermentation platform;    (C) spreading bacteria in the prepared chicken manure, stirring uniformly, adjusting the water content of the chicken manure to 60%, and processing the other four stack chicken manure using the same method to deal with another four stack chicken manure;    (D) after composting, automatic heating to above 55 degrees C for 5-7 days, about three days turning over a stack of 7-10 days fermentation, dropping the temperature below the natural 50 degrees C, adding mixture with 5-8 kg strain, and stirring with 50% water; and    (E) drying the fermented material, crushing and sieving to obtained the finished product and packaging.
NOVELTY - A fertilizer comprises 60-80 pts. wt. poultry manure, 15-20 pts. wt. borax, 9-14 pts. wt. mycelium, 8-12 pts. wt. peat soil, 3-5 pts. wt. egg shell powder, 4-6 pts. wt. mushroom residue and 0.3-0.8 pt. wt. effective microorganisms.    USE - Fertilizer used for wheat.    ADVANTAGE - The fertilizer is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising mixing raw materials, adjusting water content to 45-55 vol.% and pH to 6-7, fermenting for 30 days, turning every 2-3 days, controlling temperature at 55-65 degrees C, screening, removing impurities, and granulating.
NOVELTY - Synthesizing rivaroxaban intermediate 4-(4-aminophenyl)-3-morpholinone comprises reacting p-nitroaniline and ethylene oxide to obtain N-(hydroxyethyl)-p-nitroaniline, performing cyclization reaction with bromoacetyl bromide to obtain 4-(4-nitro phenyl)-3-morpholone, adding iron powder and performing reduction reaction.    USE - The method is useful for synthesizing rivaroxaban intermediate 4-(4-aminophenyl)-3-morpholinone (claimed).    ADVANTAGE - The method utilizes raw materials, which are economical and easy to obtain, is simple and avoids industrial nitration, and is suitable for industrial production and is environmentally friendly.
NOVELTY - A hydrogen-rich gas preparation method involves collecting waste, sorting organic component, baking at 105 degrees C for 24 hours, drying organic component, crushing into 3 parts, controlling organic compound and calcium oxide mass ratio at 95:5, 90:10 and 85:15, performing extrusion molding, treating resultant product in a fixed bed gasification device at 700-900 degrees C for 4 hours to obtain finished product.    USE - Method for preparing hydrogen-rich gas.    ADVANTAGE - The method enables preparing hydrogen-rich gas in a simple, effective and eco-friendly manner.
NOVELTY - Feed composition preparation involves collecting organic waste with impurities. The organic waste is crushed into powder. Water content of particles of organic waste is 50-60%. Crushed organic waste particles (60-90wt.%) are mixed with additives (10-40wt.%) and beneficial microorganism strain (0.1-1wt.%). Obtained mixture is fermented at 25-45 degrees C for 7-15 days in anaerobic or aerobic condition to obtain final product.    USE - Method for preparing feed composition for insects (claimed).    ADVANTAGE - The method ensures preparation of feed composition with biological safety in a timesaving and cost-effective manner.
NOVELTY - The method involves removing gross floater and non-solubility suspended substance in waste water. The organic acid is decomposed into methane and carbon dioxide for removing floating oil in ABR reactor (4) during anaerobic processing process. The ammonia nitrogen in waste water is removed to obtain purified water, by taking water in sedimentation tank (8). The water in coagulation reaction tank (9) is filtered by filtering cloth, for removing total phosphorus. The anaerobic methane generated in ABR reactor is processed in marsh gas desulfurization and exhaust gas burning system (16).    USE - High-oil food processing wastewater treatment method for removing animal and vegetable oil and organic pollutant in waste water.    ADVANTAGE - The food processing waste water can be processed easily and efficiently, so as to remove the animal oil, vegetable oil and organic pollutant in the waste water. The water quality can be improved. The calcium ion and aluminum ion can be added in the wastewater, so as to generate the phosphate precipitate and to form flocculation particles. The micro-bubbles can be generated in flotation tank. The residual oil impurity adhered to the flocculation particle can be removed easily. The standard oil index can be satisfied. The biochemical processing load can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the high-oil food processing wastewater treatment device. (Drawing includes non-English language text)    Coarse screen (1)    ABR reactor (4)    Sedimentation tank (8)    Coagulation reaction tank (9)    Marsh gas desulfurization and exhaust gas burning system (16)
NOVELTY - A beraprost sodium compound, is new.    USE - The beraprost sodium is useful for beraprost sodium element or intermediates (claimed).    ADVANTAGE - The preparation method provides mild reaction condition. It can avoid toxic reagent. The yield is high, and it is suitable for industrial production.    DETAILED DESCRIPTION - A beraprost sodium compound of formula I, is new.    R1=methyl or ethyl;    R2=H, 1-4C alkoxyalkyl or tetrahydropyranyl; and    R=hydrocarbyl substituted silicon group, -CHO, or -CH2OH.    INDEPENDENT CLAIMS are:    (1) a method for preparing beraprost sodium compound; and    (2) a method for preparing beraprost sodium intermediates involving: (a) reacting a compound of formula Id compound below to obtain a compound of formula III as intermediate; (b) reacting compound of formula III with a reducing agent to obtain a compound of formula IV as intermediate; and (c) hydrolysis of compound of formula IV by alkaline condition to obtain beraprost sodium intermediates.    .
NOVELTY - The method involves separating bamboo crumbs and bamboo oil-gas to obtain bamboo oil. Distilling process is performed for the bamboo oil. Oil residue is put into carbonization furnace and heated to obtain bamboo carbide, which is collected. Flue gas cooling, filtering, separating and purifying processes are performed to obtain tar and gas. Bamboo charcoal compound is made into bamboo charcoal powder material.    USE - Environment-friendly value-added bamboo utilization method.    ADVANTAGE - The method enables improving bamboo resource utilization efficiency to about 15 %, and practicability of bamboo, avoiding generation of bamboo scrap and environmental pollution and reducing bamboo processing cost.
NOVELTY - The device has housing (212) connected with spiral material input machine (210), lower storage bin (217) and spiral material output machine (218). The housing includes a rotating shaft (207) connected with a drive motor (201). A material grid plate (208) is provided in upper wall of the housing. Several tower plates (213) are connected in series between the rotating shaft and grid plate. A drying component of housing is provided with several heating coils connected in series between rotating shaft and heating plate (214) connected with a steam inlet (216) and steam outlet (211).    USE - Continuous solid fermentation material separation device for preparing fuel ethanol.    ADVANTAGE - The environment-friendly nature of the solid fermentation material separation device can be enhanced while significantly reducing the cost of preparing the fuel ethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous sold fermentation material separation device.    Drive motor (201)    Rotating shaft (207)    Material grid plate (208)    Spiral material input machine (210)    Steam outlet (211)    Housing (212)    Tower plates (213)    Heating plate (214)    Steam inlet (216)    Lower storage bin (217)    Spiral material output machine (218)
NOVELTY - The device has feeding pipe (1) that is located in upper end of fermentation tank (14). A discharge pipe (10) is connected with lower portion of discharging chamber (8). The tank is connected with gas storage chamber (5), via gas-guide tube (3). The gas storage chamber is set with exhaust pipe (7). The gas-guide tube and discharging pipe are set with upper valve (9). A distributor (13) is located in tank close to bottom of feeding pipe. A stirring rod (12) is set at center of tank, and heat exchanger (11) is located in tank.    USE - Device for fermenting marsh gas such as methane gas (claimed), for use in agricultural field.    ADVANTAGE - The structure of the device for fermenting the marsh gas is simplified, and the easy operation of the device is achieved. The production efficiency of the device is effectively improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for fermenting the marsh gas.    Feeding pipe (1)    Gas-guide tube (3)    Gas storage chamber (5)    Exhaust pipe (7)    Discharging chamber (8)    Upper valve (9)    Discharge pipe (10)    Heat exchanger (11)    Stirring rod (12)    Distributor (13)    Fermentation tank (14)
NOVELTY - Producing ethanol from corn straw comprises crushing straw, pre-dipping the crushed straw with acid to impregnate, carrying out steam explosion and steam blasting, saccharifying, fermenting and distilling steam blasting in a fermentation system, applying the appropriate genetically engineering bacteria or yeast and enzyme, distilling to obtain ethanol, recycling carbon dioxide produced by fermentation, separating the fermentation product to obtain solid residue and fermentation liquid, drying obtained solid residue into the biomass combustion power plant.    USE - The method is useful for producing ethanol from corn straw (claimed).    DETAILED DESCRIPTION - Producing ethanol from corn straw comprises crushing straw, pre-dipping the crushed straw with acid to impregnate for one time, carrying out steam explosion and steam blasting, synchronously saccharifying, fermenting and distilling steam blasting in a fermentation system to form straw pulp of 10-20%, applying the appropriate genetically engineering bacteria or yeast and enzyme into the pulp and then distilling to obtain ethanol, recycling carbon dioxide produced by fermentation, separating the fermentation product to obtain solid residue and fermentation liquid, drying obtained solid residue into the biomass combustion power plant, carrying out anaerobic fermentation, and collecting biogas.
NOVELTY - Preparing 2' 3'-di-o-acetyl-5'-deoxy-5-fluorocytidine comprises reacting 5-fluorin cell pyrimidine (5-f Iuorocytosine) as substrate with 5-ribose-1-(5-deoxyribose-1-phosphate) nucleoside using an pyrimidine nucleoside phosphorylase (EC2.4.2.2) as enzyme catalyst.    USE - The method is useful for preparing 2' 3'-di-o-acetyl-5'-deoxy-5-fluorocytidine (claimed).    ADVANTAGE - The method is capable of preparing industrial production with high yield, quality and good stability in a simple and eco-friendly manner.
NOVELTY - A nanocarbon Eucalyptus fertilizer comprises 20-40 wt.% urea, 5-16 wt.% calcium phosphate, 5-16 wt.% magnesium sulfate, 5-16 wt.% phosphorus, 18-45 wt.% potassium chloride, 1-10 wt.% borax, 1-10 wt.% zinc sulfate, 3-16 wt.% peat, 20-40 wt.% minerals, 1-10 wt.% functional bacterial liquid and 1-10 wt.% carbon nanotube.    USE - Nanocarbon Eucalyptus fertilizer.    ADVANTAGE - The fertilizer improves the quality of Eucalyptus and soil, prevents cadmium contamination in soil, and reduces production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of nanocarbon Eucalyptus fertilizer comprising stirring raw materials for 1-2 hours in conical mixer, adding functional bacteria liquid, stirring, pouring into disc pelletizer, polishing film, passing through vibration screen with 0.1-1.5 mm diameter, drying for 20-40 minutes, cooling in belt conveyor, sieving and packing.
NOVELTY - This utility model relates to one kind of waste gas harmless processing system of waste gas through different processing stages taking it's decomposition processing, comprising a waste gas collecting system's waste gas, waste gas pressure mixing system pre -'s waste gas catalytic system taking the waste gas catalytic processing, a gas detecting system for detecting processing's exhaust gas, adjusting the system carrying liquid's pH value adjusting processing, an air pressurization system's processing waste gas, biochemical system to exhaust gas and carried liquid's taking biochemical processing physical and chemical system for carrying liquid taking physical and chemical separation processing, liquid system carrying liquid re-distributing the 's cycle processing, sludge dehydrating and drying the system's processing. The utility model capable of taking various waste gases is completely harmless processing's,'s waste gas after processing exceeds all kinds of current waste gas discharge standard, liquid can be used circularly, processing flow is simple operation, low operation cost, little in investment cost, all kinds of waste gas can effectively processing.
NOVELTY - One of the overturning device for hydraulic biogas pool, comprising a fermentation chamber and water pressure, said fermentation room and the bottom of the water's pressure to the rubble concrete layer and the first sealing layer,'s wall between the fermentation chamber and the water pressure from outside to inside a first structure layer, concrete layer, layer, a second sealing layer's tank cover between the fermentation chamber and the water pressure from outside to inside in turn is the third sealing layer, the second structure layer, reinforcing steel bar concrete layer. Adopting said structure, time table's layer at the bottom of the fermentation chamber and water pressure is rubble concrete layer which can increase the fermentation room and water pressure between the bottom under the condition of effectively controlling cost's's strength.
NOVELTY - Manufacturing concentrated liquid fertilizer using butchery blood, comprises (S3) refining butchery blood with a crusher to obtain fine blood, (S5) placing the fine blood and enzymes in a sterile fermentation tank, sterilizing the mixture with ultraviolet rays at 50-65 degrees C, and fermenting to obtain fermented blood, and (S7) placing the fermented blood in a concentration tank, stirring, removing moisture under vacuum generated by a vacuum generator, and concentrating the ratio of amino acids higher than the fermented blood.    USE - The method is useful for manufacturing concentrated liquid fertilizer using butchery blood (claimed).    ADVANTAGE - The method recycles the discarded butchery blood, and is environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for manufacturing concentrated liquid fertilizer using butchery blood (Drawing includes non-English language text).    Butchery blood preparing step (S1)    Fine blood obtaining step (S3)    Fermenting step (S5)    Concentrating step (S7)    Washing step (S11)
NOVELTY - A wood vinegar tar removing method involves adapting process of oxygen-free carbonization of plants, and device for producing less tar content with less impurity and smoke.    USE - Method for removing wood vinegar tar.    ADVANTAGE - The method enables removing wood vinegar tar in an effective manner.
NOVELTY - Preparing pure diarylpyrimidin-2(1H)-ones (A) comprises: mixing aldehyde (X1), ketone (Y1) and urea (Z1) with at least one large pore zeolite in a solvent to get the reaction mixture; refluxing the reaction mixture to get the crude (A) in a reaction mixture; filtering the reaction mixture and evaporating the solvent from the reaction mixture to give crude (A); and crystallizing crude (A) with solvent to obtain pure (A).    USE - The process is useful for preparing pure diarylpyrimidin-2(1H)-ones (claimed) which is useful to treating B16 melanoma and P388 leukemia or antagonize cell proliferation and induce cell differentiation. No biological data given.    ADVANTAGE - The process: provides (A) with high yield; is safe, environment-friendly, industry viable; and utilizes the zeolite catalyst that is economically and environmentally feasible.    DETAILED DESCRIPTION - Preparing pure diarylpyrimidin-2(1H)-ones of formula (A) comprises: mixing aldehyde of formula (X1), ketone of formula (Y1) and urea of formula (Z1) with at least one large pore zeolite in a solvent to get the reaction mixture; refluxing the reaction mixture to get the crude (A) in a reaction mixture; filtering the reaction mixture and evaporating the solvent from the reaction mixture to give crude (A); and crystallizing crude (A) with solvent to obtain pure (A).    Ar1, Ar11=aryl (optionally substituted by phenyl, 4-hydroxyphenyl, 3- nitrophenyl, 4-fluorophenyl, 2-hydroxyphenyl, 3-methoxyphenyl, 4-methoxyphenyl, 4-chlorophenyl, 4-bromophenyl or 4-iodophenyl); and    M=O or S.
NOVELTY - Preparing dihydropyrimidin-2(H)-one compounds (X) comprises: mixing urea compounds (B1), ethylacetoacetate (C1) and aldehyde compounds (A1) with at least one large pore zeolite in a solvent to get the reaction mixture; refluxing reaction mixture to get the crude (X) in a reaction mixture; filtering the reaction mixture and evaporating the solvent from the reaction mixture to give (X); and crystallizing crude (X) with solvent to obtain pure (X).    USE - The process is useful for preparing X (claimed) that are used as antihypertensive and antiinflammatory agents. No biological data given.    ADVANTAGE - The process is safe, environmentally friendly and industry viable.    DETAILED DESCRIPTION - Preparing dihydropyrimidin-2(H)-one compounds of formula (X) comprises: mixing urea compounds of formula (B1), ethylacetoacetate of formula (C1) and aldehyde compounds of formula (A1) with at least one large pore zeolite in a solvent to get the reaction mixture; refluxing reaction mixture to get the crude (X) in a reaction mixture; filtering the reaction mixture and evaporating the solvent from the reaction mixture to give (X); and crystallizing crude (X) with solvent to obtain pure (X).    R=1-4C alkyl, aryl, substituted aryl (phenyl, 4-hydroxyphenyl, 3-nitrophenyl, 4-fluoro phenyl, 2-hydroxyphenyl, 3-methoxy phenyl, 4-methoxyphenyl, 4-chlorophenyl, 4-bromophenyl or 4-iodo phenyl) or 2-substituted C 9H 5N (2-chloro-C 9H 5N or 2-bromo-C 9H 5N); and    M1=O or S.
NOVELTY - Degradation of 2,4-dichlorophenol with sodium hydrosulfide promoted Phanerochaete chrysosporium comprises adding Phanerochaete chrysosporium in liquid culture medium, oscillating, adding sodium hydrosulfide, filtering, processing residue, adding to 2,4-dicholorophenol containing wastewater and reacting for not less than 24 hours.    USE - Method for degrading 2,4-dichlorophenol with sodium hydrosulfide promoted Phanerochaete chrysosporium (claimed).    ADVANTAGE - The simple and convenient method shortens degradation time.
NOVELTY - Removal of azo dyes in wastewater with Pseudomonas aeruginosa comprises culturing Pseudomonas aeruginosa to log phase, centrifuging, removing supernatant, washing with sterile distilled water, resuspending bacteria in phosphate buffer saline, placing bacteria into tapered flask, adding azo dyes and stirring at constant temperature under aerobic condition.    USE - Method for removing azo dyes in wastewater with Pseudomonas aeruginosa.    ADVANTAGE - The method ensures fast removal of azo dyes.
NOVELTY - Microbial fermentation comprises crushing various materials, granulating, adding composite strain bacteria and performing aerobic fermentation.    USE - Microbial fermentation used for reducing water content of sludge dewatering (claimed) and as organic fertilizer.    ADVANTAGE - Method has low energy consumption, low material consumption and reduces sludge moisture content to 30%.
NOVELTY - Preparing 4,4'-dihydroxybenzophenone, comprises using p-hydroxybenzoic acid and phenol as raw materials, phosphorus oxychloride and aluminum trichloride as catalyst, and dimethyl sulfoxide as solvent, and carrying out synthesis reaction to prepare 4,4'-dihydroxybenzophenone.    USE - The method is useful for preparing 4,4'-dihydroxybenzophenone (claimed).    ADVANTAGE - The method reduces the production cost; shortens the production period; does not pollute the environment; does not generate waste in the reaction process, thus reducing the environmental pollution.
NOVELTY - The method involves crushing cane root to obtain a particle. Ash and water are separated. A semi-finished product is crushed by an auger conveyor machine. The semi-finished product is distilled at temperature of 10 degrees Celsius. The semi-finished product is cooled for about 14-15hours. Wood tar and methane are produced during carbonization process. The wood tar and the methane are condensed and stored in a marsh gas storage tank. A sweet potato sunflower leaf is removed and crushed. The crushed sweet potato sunflower leaf is placed in the marsh gas storage tank.    USE - Method for combinedly producing wood tar and methane by processing environment-friendly machine-made carbon and sweet potato sunflower leaf.    ADVANTAGE - The method enables utilizing a wood crushing machine for crushing the cane to obtain high efficient particle. The method enables producing large amount of the wood tar and the methane and improving mechanical properties of the wood tar and the methane by performing long-time combustion process. The method enables utilizing the wood tar as fuel, thus realizing environment-friendly wood tar production and reducing production cost. The method enables producing a rich raw material during methane production process for preventing a plant from being invaded due to disaster. The method enables generating 200-250 kg of the wood tar by utilizing a ton of the semi-finished product.
NOVELTY - The system has a gas-solid separator connected with an upper part of a lifting tube burner by a pipeline. A lower part of a hot carrier separator is connected with the lifting tube burner by a hot carrier lifting tube. The lifting tube burner is connected with a first biomass feeder. A carbon powder storage bunker is connected with a second biomass feeder. An upper part of a V-shaped descending pipe reactor is connected with a third biomass feeder. The lifting tube burner is provided with solid particles of a hot carrier.    USE - Hot carrier self-circulation heating-type agriculture and forestry waste pyrolysis liquefaction system.    ADVANTAGE - The system reduces renewable energy utilization rate, and is stable to operate. The system has low processing cost and high liquefaction efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hot carrier self-circulation heating-type agriculture and forestry waste pyrolysis liquefaction system. ' (Drawing includes non-English language text) '.
NOVELTY - An Acinetobacter sp. TN-14 strain deposited under CCTCC NO. M2013247 on June 5 2013, for producing flocculant for high efficiency denitrification and dephosphorization of nitrogen, is new.    USE - The Acinetobacter sp. TN-14 strain is useful for producing flocculant for high efficiency denitrification and dephosphorization of nitrogen (claimed).    ADVANTAGE - The strains provide high total nitrogen removal, and high flocculation rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for using the strain for high efficiency denitrification and dephosphorization of nitrogen comprising applying and processing the strain to domestic sewage; and using the ferment culture medium or replacing culture medium with biological flocculating agent.
NOVELTY - A one aerobic microorganism processing sewage, wherein it comprises a machine frame, is set on the bearing's frame middle part, the rotating shaft hollow is set on the bearing's's upper, upper's bracket is fixed on the rotating shaft and fan blade is set on the machine frame and the bracket and fan blade upper surface's aerobic bio-membrane bed, upper bracket is provided with a plurality of nozzle through the rotating shaft hollow and water supply device's's, inclined downwards, each nozzle to the axis is inclined direction's's circle's centre line are the same. The utility model compared with the existing technology, it has no need to pumping power supply it's oxygen and energy-saving.
NOVELTY - The system has a processor (1) that processes and outputs organic waste to a composting process unit (2). The composting process unit separates solid and liquid contents from the organic waste. A nitrification basin (206) processes solid and liquid contents separated from the organic waste. A digeater (403) of a biogas production process unit (4) processes fire-extinguishing sap generated from a digestion tank to produce biogas or liquefied fertilizer from the organic waste.    USE - System for recycling organic waste e.g. livestock execration obtained from stockbreeding farmhouse.    ADVANTAGE - The organic waste can be processed effectively. The by-product compost can be derived efficiently from the organic waste. The recycling system is environment-friendly. The generation of drug sludge from organic waste can be prevented. The recycling efficiency of organic waste can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for recycling organic waste. (Drawing includes non-English language text)    Processor (1)    Composting process unit (2)    Biogas production process unit (4)    Nitrification basin (206)    Digeater (403)
NOVELTY - Lignin fuel is prepared by subjecting wood residue in conveying device, heating at 0.5-2.5 MPa for 1-5 minutes, extracting with less than or equal to 85% aqueous acid solution to obtain hemicellulose-rich precipitate, adding 4-10% alkali, heating at 60-130 degrees C for 0.5-2 hours, subjecting to anaerobic fermentation to obtain crude liquid, depositing, filtering, activating, forming film, and drying.    USE - Method for preparation of lignin fuel (claimed).    ADVANTAGE - The preparation method is comprehensive and efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of preparation of lignin fuel. (Drawing includes non-English language text).
NOVELTY - Method for producing lignin, involves (a) pre-processing raw material, and steaming the material continuously, washing, separating solid-liquid and removing hemicellulose and polysaccharide, (b) adding alkali solution to solid material, and steaming, and again separating solid-liquid and removing cellulose to obtain lignin raw liquid, and (c) adding calcium hydroxide to lignin raw liquid for flocculation, and filtering the liquid and concentrating, evaporating and spray drying and processing to obtain the product.    USE - The method is useful for producing lignin (claimed) and marsh gas and biofuel.    ADVANTAGE - The method is cost-effective by utilizing agricultural and forest waste as raw materials, and capable for producing 0.15 ton.    DETAILED DESCRIPTION - Method for producing lignin, involves (a) collecting fibre as raw material, pre-processing the material by feeding the material to separating device using conveying device, and steaming the material continuously at 1-2 MPa for 1-5 minutes, and washing the steamed material, separating solid-liquid and removing hemicellulose and polysaccharide, (b) adding 4-10% alkali solution, and steaming at 80-130 degrees C for 0.5-2 hours, and again separating solid-liquid and removing cellulose to obtain lignin raw liquid, and (c) adding 10-100 parts per million calcium hydroxide to lignin raw liquid for flocculation, and filtering the liquid using filtering device with 20 mu m membrane for removing impurities and concentrating the filtrate, evaporating and spray drying and processing to obtain the product.
NOVELTY - Microbial fuel cell driven capacitive deionization system comprises microbial fuel cell system, capacitive deionizing system and external circuit connector. The continuous operation of microbial fuel cell comprises treating sewage and providing stable voltage for capacitive deionization device.    USE - Microbial fuel cell driven capacitive deionization system used for desalination to control pollution and recycling energy from sewage processing systems.    ADVANTAGE - The system reduces energy consumption.
NOVELTY - Phosphorus removal agent comprises substrate carrier water, 2-7 wt.% alcohol, 10-25 wt.% dendrobe extract, 0.1-1 wt.% titanium dioxide nanoparticles, 0.1-3 wt.% chitosan, 0.1-2 wt.% citric acid and 0.01-0.1 wt.% polyphosphate-accumulating bacteria HJP07.    USE - Phosphorus removal agent used for rural domestic sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of phosphorus removal agent comprising adding agent into pre-sedimentation tank, pumping rural domestic sewage at constant flow rate, setting electrode and solar panel, and treating.
NOVELTY - The method involves drying bamboo by utilizing a bamboo drier. Exhaust gas is passed into a combustion chamber. The combustion chamber is connected with a drying machine. A rotary kiln drier is connected with a dry distillation furnace. Combustible gas is supplied to a multi-section furnace. Carbonization process is performed. A burner is connected with the combustion chamber. A quenching groove is formed in the bamboo drier that is utilized for drying bamboo charcoal. Carbonization operation temperature is maintained at 350 to 700 degrees Celsius.    USE - Bamboo charcoal manufacturing method.    ADVANTAGE - The method enables improving production efficiency and environment protection performance and saving energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bamboo charcoal manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a bamboo charcoal manufacturing device.'(Drawing includes non-English language text)'
NOVELTY - Synchronous processing of municipal sewage and grease accumulation using fresh algae, where the fresh algae is Scenedesmus obliquus PF3 with a preservation number of CGMCC No. 8015.    USE - The method is useful for synchronous processing of municipal sewage and grease accumulation of inclined grid fresh algae (claimed).    ADVANTAGE - The fresh algae have strong anti-pollution ability and can be efficiently used in controlling sewage grease.
NOVELTY - Heterotrophic nitrifying aerobic denitrifying fungi strain preserved under China microorganism strain preservation management committee common microorganism centre with preservation number of CGMCC N0.7656, is new.    USE - The heterotrophic nitrifying aerobic denitrifying fungi strain is useful in sewage processing (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of heterotrophic nitrifying aerobic denitrifying fungi strain for sewage processing comprising: inoculating fungi strain into a culture medium comprising 1000 ml of water, 9.782 g of sucrose, 1.888 g of ammonium sulfate, 1 g of potassium phosphate, 0.5 g of potassium chloride, 0.5 g of magnesium sulfate heptahydrate, 0.01 g of iron(II) sulfate heptahydrate; maintaining pH of the culture medium at 7-7.4; and adding bacterial liquid into sewage wastewater.
NOVELTY - Chemical modification method of fiber immobilized carrier involves preparing polyethylene modified carrier by immersing fiber immobilized carrier in polyethylene imine solution, and soaking the prepared polyethylene modified carrier in glutaraldehyde solution such that polyethylene imine and glutaraldehyde are reacted. The fiber immobilized carrier is plant straw, preferably sugar cane bagasse, straw and corn straw.    USE - Chemical modification method of fiber immobilized carrier used for preparation of butanol (claimed).
NOVELTY - Producing hydrogen by straw fermentation comprises: (1) taking the straw steam explosion pre-treatment; and (2) placing pre-treated straw and anaerobic sludge into hydrogen-producing reactor, and then taking anaerobic fermentation to prepare hydrogen, where in step (2), the aldehyde fermentation inhibitor is used with different concentrations by adjusting the hydrogen producing reaction, the temperature is 30-50 degrees C, the time is 1-5 days, the aldehyde fermentation inhibitor is 5-hydroxymethyl furfural (5-HMF) and/or furfural (FUR).    USE - The method is useful for producing hydrogen by straw fermentation (claimed).    ADVANTAGE - The method does not need to directly take detoxification-fermentation to generate hydrogen.
NOVELTY - Fermenting and producing methane using rumen microorganism, involves taking biomass waste, inoculating gastric juice containing microbial flora to biomass waste, adding inoculated material to anaerobic fermentation reactor, collecting culture, fermenting to generate methane gas, performing anaerobic fermentation in reactor to obtain product, maintaining water content, and collecting generated biogas.    USE - The method is useful for fermenting and producing methane using rumen microorganism (claimed).    ADVANTAGE - The method improves digestibility by 10-20%, shortens fermentation time by 3-10 days, enhances methane production efficiency to 210-250 ml/g, produces gas that can be recycled for processing, and utilizes left over as organic fertilizer.    DETAILED DESCRIPTION - Method for fermenting and producing methane using rumen microorganism, involves taking biomass waste, inoculating gastric juice containing microbial flora to biomass waste, adding inoculated material to anaerobic fermentation reactor, collecting culture after 1-10 days, where solid content of culture is 1-5%, fermenting for 10-25 days to generate methane gas, maintaining hydrogen content to less than 2%, performing anaerobic fermentation in reactor to obtain product with solid content of 5-10%, maintaining water content for 6-20 days, and collecting generated biogas, where the reactor utilizes biomass substrate of concentration 10-100 g/l and pH is 6-70, the temperature is 30-45 degrees C, and the stirring speed is 50-150 revolutions/minute (rpm).
NOVELTY - Acid production method involves taking sludge as raw material, adjusting the concentration of sludge by adding sodium hydroxide, centrifuging the resultant product to obtain supernatant as anaerobic fermentation substrate, adding hydrated metal compound composition, and then carrying out fermentation process.    USE - Acid production method (claimed).    ADVANTAGE - The method economically provides acid with high conversion rate under short period of time.
NOVELTY - Production of ethanol and lactic acid involves sorting kitchen garage, adding water and mixed flora to waste, fermenting and obtaining ethanol, adding water, mixed bacteria, calcium carbonate and lactic acid fermentation strain to fermentation residue, fermenting at 30 degrees C and obtaining lactic acid. The mixed bacteria are Pichia pastoris, Aspergillus niger, Rhizopus, Saccharomyces cerevisiae or Trichoderma harzianum. The lactic acid fermentation strain is Weissella sp., Lactobacillus plantarum and Rhizopus.    USE - Production of ethanol and lactic acid (claimed).    ADVANTAGE - The method efficiently and economically provides ethanol and lactic acid using simple process.
NOVELTY - The utility model claims one protecting plate type top pressure glass steel marsh gas tank belongs to marsh gas tank technology field. This utility model's protective plate type top pressure glass fibre reinforced plastic biomass pool, comprising a lower pool, upper pool and water pressure chamber, said upper tank's lower jaw and the lower pool's upper opening is hermetically connected to form a hollow cavity, said water pressure chamber is installed on the upper top part, upper, upper tank is provided with a feeding channel and a discharging channel, is provided with a gas-guide tube on the top part's upper tank's top part between said water pressure is integrated structure's plate, area between the water pressure chamber's upper tank and the water pressure room is set in said's is divided into feeding area and the discharging area, said upper plate is provided with a feeding port and a discharging port, wherein the feeding port, the feeding area and feeding channel are connected with each other, wherein a discharging port, a discharging region and discharging channel are connected with each other. This utility model's protective plate type top pressure glass fibre reinforced plastic biomass pool, the water pressure chamber safety protection improves strength and to enhance the protection function, the product is beautiful.
NOVELTY - The method involves collecting malodorous gas in a buffer surge tank. An active sludge absorption process is performed on a top part of an absorption tower. Active sludge is collected. Malodorous gas is discharged in an aerobic tank. A biochemical degradation process is performed on a bottom part of the absorption tower. Pressure of the buffer surge tank is measured. Pressure of the buffer surge tank is 0.03 to 0.06 MPa. The absorption tower is provided with a gas distributor.    USE - Method for collecting and purifying malodorous gas in a sewage processing field.    ADVANTAGE - The method enables accurately collecting and purifying malodorous gas in the buffer surge tank through a draught fan according to requirement in a simple manner, avoiding need of utilizing additional processing device and reducing collecting and purifying malodorous gas cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a method for collecting and purifying malodorous gas in a sewage processing field.
NOVELTY - A deep-underground soil percolation system sewage processing disposal device comprises water inlet pipe (2), water outlet pipe (7) and non-soil filler material with different grain diameters for upper filler layer (4), middle filler layer (5) and lower filler layer (6).    USE - Deep-underground soil percolation system sewage processing disposal device used for municipal sewage, and rural centralized and decentralized domestic sewage.    ADVANTAGE - The device has good denitrification efficiency, stable effect, low operation cost, and convenient and simple management and maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of deep-underground soil percolation system sewage processing disposal device.    Water inlet pipe (2)    Upper filler layer (4)    Middle filler layer (5)    Lower filler layer (6)    Water outlet pipe (7)
NOVELTY - Composition comprises 100 pts. wt. mudstone, 2-5 pts. wt. calcium nitrate, 0.002-0.003 pts. wt. cobalt, 0.0015-0.002 pts. wt. germanium, and 0.002-0.0025 pts. wt. selenium as natural mineral, which ensures survival of natural microbes and inoculated with mixture of Bacillus firmus (NCIMB 9366T) and Bacillus cereus (ATCC14579T).    USE - The composition is useful for preventing red pepper disease (claimed), preferably Phytophthora blight and anthracnose.    ADVANTAGE - The composition prevents agricultural chemical poisoning and environmental pollution or toxicity caused by agricultural chemical residue discharge, and cultivates blight-tolerant crops by using mineral components without weakening crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for red pepper crop cultivation, comprising performing top dressing fertilizer application on the red pepper young plants using the composition for 5-6 times, and performing top dressing fertilizer application once per week until the peppers are harvested; or comprising adopting a combination of fertilization and irrigation during top dressing fertilizer application.
NOVELTY - A Penicillium strain, i.e. Penicillium purpurogenum BJHY-501 strains deposited in the China General Microbiology Centre Management Committee, the accession number of CGMCC 8036, accession date of August 16, 2013, is new.    USE - Penicillium strain, i.e. Penicillium purpurogenum BJHY-501 strain for treating waste water and odor pollution in the field (claimed)    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a biological agent comprising Penicillium strain (2) a method for degrading sewage and odor, which involves utilizing the Penicillium strain with the ammonia nitrogen.
NOVELTY - The utility model claims one universal and sewage purifying system, comprising a core component, said core component comprises a motor, a reverse umbrella-shaped gas-liquid transmission device, a guide lifting cylinder, microorganism growth carrier and a bracket, wherein said electric motor is fixed on the upper bracket, inverted gas-liquid transmission device with motor, the motor is driven to rotate by a motor, and inverted gas-liquid transfer device's umbrella the guide lifting cylinder's top opening at the lower end, a guide lifting cylinder is fixed on the upper bracket, the growth carrier is provided is connected with the bracket or guide lifting cylinder on the guide lifting cylinder. The utility model claims universal and medium sewage purification system's efficiency, low cost and convenient to maintain.
NOVELTY - A plurality of The utility model claims one intestinal marsh gas generator system, belonging to the field of methane producing device, comprising a feeding device, a multi-inlet type ferment intestinal pipeline, marsh gas collecting device, said feeding device is mainly composed of a multi-inlet multi-drain collector is set in the high position's, collector is connected with the sewage collecting pipe's, the total feeding pipe, said intestinal type fermentation pipeline comprises a deep 's underground storage tube chamber, fermenting the pipeline's multi-layer superposed as bending the intestinal tract's underground's spiral, said feeding port is connected with the total feeding pipe's said fermentation pipeline; said marsh gas collecting device comprises a marsh gas collecting pipe, an air storage part, said marsh gas collecting pipe is provided with multiple respectively from the upper layer's fermentation pipeline's. Feces and organic material can make the complete fermentation, and realizes automatic feeding, automatic discharging, automatic material separation, automatic conveying to the head field, no agglomeration, no residue, energy-saving and environment-friendly.
NOVELTY - The utility model claims one soft bag for marsh gas marsh gas leading-out structure, one end and comprises a soft methane bag's lining tube, the lining tube is soft marsh gas bag's connection guiding head, one end of the liner tube is soft marsh gas bag's outside cover and the air through the sealing bend head is connected with the lower end of the sling chain sealing cover far away from one side of air elbow air flow direction, the chain's end is fixed on the upper top point, the guide head is chain traction markup's soft methane bag surface is provided with a tension ring. Device provided by this utility model overcomes the deficiency existing technology's, the structure is simple, the cost is low, when the suction to the chain caused by the sealing cover, the guide head guide hole and the central axis there is a certain angle, it is easy to stick the soft methane bag surface, naturally to the air's effect to ensure the biogas slurry's will not happen in the soft methane bag also pumping out's.
NOVELTY - Denitrifying municipal sewage, comprises detecting biological oxygen demand 5 (BOD5)/total Kjeldahl nitrogen (TKN) value of sewage inflow, and adding organic matter into sewage, when the BOD5/TKN value is not less than 4.    USE - The method is useful for denitrifying municipal sewage (claimed).    ADVANTAGE - The method supplements inadequate carbon source, while processing sewage in a primary settling tank, shortens the residence time of the effluent in the primary settling tank or directly across the primary settling tank, maximizes the biological removal of nitrogen entering the sewage system BOD/TKN value, and reduces the utilization amount of organic matter (claimed); and has simple technique, convenient operation procedure, and good denitrifying effect.
NOVELTY - Reducing adverse effect of nano-material in biological phosphorus and nitrogen removal treatment of wastewater comprises (i) carrying out anaerobic fermentation of organic waste containing propionic acid and protein at 30-50 degrees C for 2-8 days; (ii) adding the resulting fermentation solution into to be processed wastewater containing nano-materials, measuring chemical oxygen demand (COD), and controlling concentration of propionic acid to be greater than 10 mg/l, and protein to be greater than 10 mg/l; and (iii) carrying out biological phosphorus and nitrogen removal treatment of wastewater.    USE - The method is useful for reducing adverse effect of nano-material in biological phosphorus and nitrogen removal treatment of wastewater (claimed).    ADVANTAGE - The method realizes reduction rate of nano-materials having adverse effects in phosphorus and nitrogen removal process by 80% and 60%.    DETAILED DESCRIPTION - Reducing adverse effect of nano-material in biological phosphorus and nitrogen removal treatment of wastewater comprises (i) carrying out anaerobic fermentation of organic waste containing propionic acid and protein at 30-50 degrees C for 2-8 days under pH condition of 9-11, where the organic waste is kitchen waste and/or sewage treatment plant residual sludge; (ii) adding the resulting fermentation solution into to be processed wastewater containing nano-materials, measuring chemical oxygen demand (COD), and controlling the concentration of propionic acid to be greater than 10 mg/l, and protein to be greater than 10 mg/l; and (iii) carrying out biological phosphorus and nitrogen removal treatment of wastewater.
NOVELTY - Comprehensive treatment of polluted river comprises (i) before flowing exogenous sewage into river, adding composite nanometer water quality conditioner and a complex microbial agent to the exogenous source sewage; (ii) adding the composite nanometer water quality conditioner and complex agent to the river sewage; (iii) cleaning the sludge part of the river, where the river always keep the bottom with a layer of precipitate, modifying the precipitate, cleaning the river sludge, and recycling; and (iv) establishing artificial landscape balance wetland surrounding the river.    USE - The method is useful for comprehensive treatment of polluted river (claimed0.    ADVANTAGE - The method: good for recovering water self-cleaning ability; can achieve lasting ecological balance of the river; establishes an artificial landscape wetland to emulate natural landscape for providing suitable growth requirements for the microorganisms; improves the soil and water purification, pollution prevention, self-balancing effect of acid rain pollution; produces quality water after river treatment; and achieves the reconstruction of ecosystems.
NOVELTY - Aquaculture water modifier comprises 45-55 wt.% ammonium phosphate, 5-20 wt.% trace elements, 10-15 wt.% fermented organic substance, 5-10 wt.% sodium humate and 10-20 wt.% amino acid. Trace element comprises iron, boron, manganese, zinc and copper inorganic salt.    USE - Aquaculture water modifier.    ADVANTAGE - The modifier increases dissolved oxygen, reduces ammonia nitrogen, nitrite content, biomass and phytoplankton in water, and improves water quality by 15-20%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of aquaculture water modifier comprising chelating microelement, mixing with amino acid, chelating for 18-32 hours at room temperature, drying, crushing and sieving to obtain material A; mixing boron, inorganic salt and sodium humate to obtain the material B; taking organic matter, inoculating at 4500-6000 g/: organic substance, fermenting at 40-65 degrees C for 100-140 hours, drying, crushing and sieving to obtain fermented organic matter; and mixing materials A and B and fermented organic matter.
NOVELTY - Double-stage immersion-type membrane bioreactor comprises a bioreactor pool divided into upper and lower tanks, a membrane separation tank set with a separator film, and a primary filter set within the bioreactor pool. The upper tank is added with microorganisms to decompose pollutants and the lower tank with absorbing filler. The sewage is introduced into the upper tank for decomposing using microorganisms, filtered through the primary filter, conveyed into the lower tank, and then conveyed into membrane separation tank under pressure difference or pumping action through the separator film.    USE - Used as a double-stage immersion-type membrane bioreactor.    ADVANTAGE - The bioreactor intercepts large grain size of sludge floccules and particles in the biological reaction tank, which reduces the pollution membrane assembly and prolongs the service life of the membrane module, improves membrane flux and water production during utilization process, and can reduce required energy and clean water for aeration and backwashing during cleaning of the membrane module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the double-stage immersion-type membrane bioreactor.
NOVELTY - Processing nitrobenzene and aniline wastewater using microorganism, comprises conveying wastewater through three sections of co-processing systems, where a first processing system includes a first facultative aerobic tank and a first aerobic tank, a second processing system includes anaerobic ammonium oxidation (Anammox) tank, and a third processing tank includes a second facultative aerobic tank and a second aerobic tank, which are respectively adding with 1-2.5 vol.% microorganism carrier and 1.5-4 vol.% environmental microbial agent.    USE - The method is useful for processing nitrobenzene and aniline wastewater using microorganism (claimed).    ADVANTAGE - The method controls total nitrogen content in nitrobenzene and aniline wastewater to less than 20 mg/l and chemical oxygen demand to less than 80 mg/l, and ensures that the indicators meet the national level emission standards, is suitable for processing biopharmaceutical wastewater, fermentation wastewater, food enterprise wastewater, refractory wastewater, municipal wastewater and domestic sewage wastewater.
NOVELTY - Preparing azasetron hydrochloride comprises (i) using methyl 6-chloro-4-methyl-3,4-dihydro-3-oxo-2H-1,4-benzoxazin-8-carboxylate, sodium hydroxide, absolute ethyl alcohol, water and hydrochloric acid to obtain methyl (2E)-3-(4-chloro-2-nitrophenyl)acrylate crude product; (ii) refining intermediate crude product to obtain azasetron hydrochloride intermediate refined product; (iii) reacting refined product with 3-aminoquinuclidine dihydrochloride, triethylamine, N-hydroxysuccinimide, N,N'-dicyclohexylcarbodiimide to obtain azasetron hydrochloride crude product; and (iv) refining.    USE - The method is useful for preparing azasetron hydrochloride (claimed).    ADVANTAGE - The method: has short synthesis route, high yield and easiness in operation; and increasing the yield by about one time.environmentally freindly    DETAILED DESCRIPTION - Preparing azasetron hydrochloride comprises (i) using methyl 6-chloro-4-methyl-3,4-dihydro-3-oxo-2H-1,4-benzoxazin-8-carboxylate, sodium hydroxide, absolute ethyl alcohol, water and hydrochloric acid to obtain methyl (2E)-3-(4-chloro-2-nitrophenyl)acrylate crude product, i.e., azasetron hydrochloride crude product; (ii) refining azasetron hydrochloride intermediate crude product by using absolute ethyl alcohol to obtain azasetron hydrochloride intermediate refined product; (iii) reacting azasetron hydrochloride intermediate refined product with 3-aminoquinuclidine dihydrochloride, triethylamine, N-hydroxysuccinimide, N,N'-dicyclohexylcarbodiimide to obtain azasetron hydrochloride crude product; and (iv) refining azasetron hydrochloride crude product by using absolute ethyl alcohol to obtain azasetron hydrochloride.
NOVELTY - Extracting humic acid with ethanol fermented sludge, comprises dehydrating ethanol fermented sludge; heating the sludge, under stirring condition adding into ozone generator, adding ozone or 30% hydrogen peroxide solution or 30% peracetic acid solution, and reacting; adding sodium hydroxide, sodium carbonate or ammonia alkaline substances into deodorized sludge solution, then adding sodium chloroacetate, and reacting, filtering, removing impurities, and collecting the solution; taking sulfuric acid, hydrochloric acid and the above filtered solution, precipitating, drying, and pulverizing.    USE - The method is useful for extracting humic acid with ethanol fermented sludge (claimed).    ADVANTAGE - The humic acid has high yield, high purity, good agricultural fertilizer balance and synergistic effect. The method improves the comprehensive utilization efficiency of ethanol fermented sludge.    DETAILED DESCRIPTION - Extracting humic acid with ethanol fermented sludge, comprises (i) dehydrating ethanol fermented sludge until the solid content is more than 20%, (ii) heating the sludge at 20-60 degrees C, under stirring condition adding into ozone generator, adding 0.5-5 wt.% ozone or 1-5 wt.% 30% hydrogen peroxide solution or 0.5-5 wt.% 30% peracetic acid solution, and reacting for 30-120 minutes; (iii) adding 5-20 wt.% sodium hydroxide, sodium carbonate or ammonia alkaline substances into deodorized sludge solution, then adding 0.1-3 wt.% sodium chloroacetate, and reacting for 30-120 minutes, filtering, removing impurities, and collecting the solution; (iv) taking sulfuric acid, hydrochloric acid and the above filtered solution, adjusting the pH to less than 7, allowing to stand, precipitating, and collecting the precipitate by filtration, drying the precipitate, pulverizing and packaging.
NOVELTY - The device has tank portion that is provided with U-shaped portion. The top end of round hole is welded with hollow circular tube. A gas guide tube is designed with several stirrers. A large tank portion is designed with cylindrical steel pipe. A detached transverse rod is arranged with bottom of tank portion feeding port. An air storage cabinet buckle is arranged in anaerobic tank. The air storage cabinet is designed with mixer.    USE - High-concentration anaerobic device of household garbage straw.    ADVANTAGE - The user convenience of high-concentration anaerobic device can be improved reliably. The production efficiency of anaerobic device can be improved. The structure of anaerobic device is simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high concentration anaerobic device.    Steel bell jar (1)    Gas pipe (4)    Automatic stirrer (7)    Automatic exhaust valve (9)    Overflow pipe (10)
NOVELTY - The garage type straw batch fermentation device has a first fermentation chamber, second fermentation chamber, third fermentation chamber, fourth fermentation chamber, fifth fermentation chamber which are provided so as to produce gas and to work independently. The design of several biogas liquid return headers (3) is provided, so as to increase yield of methane. The combination between five fermentation chambers is provided to produce gas.    USE - Garage type straw batch fermentation device.    ADVANTAGE - The production efficiency of fermentation device is improved, and the structure of fermentation device is simplified. The adaptability of fermentation device can be improved, and environment and economy can be protected.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the garage type straw batch fermentation device.    Return pipe (2)    Biogas liquid return header (3)    Liquid spray pipe (4)    Flow channel (5)    Spray pump (6)
NOVELTY - Chlorella sp. (PF2) strain (CGMCC No.: 8014) preserved in Chinese Culture Collection Management Committee General Microbiology Centre, on 30 July 2013, is new.    USE - For microalgae biodiesel production systems and municipal sewage treatment system (claimed).    ADVANTAGE - The Chlorella sp. (PF2) strain has strong anti-pollution capability.
NOVELTY - A humic acid degradable strain (CGMCC NO: 6564) isolated from Shanghai biological activated carbon filter works, is new.    USE - The strain is useful for degrading humic acid in micro-polluted water.    ADVANTAGE - The strain has micropolluted water chemical oxygen demand removal rate of 33.8% and UV254 removing rate of 48.1%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of screening humic acid degradable strain, which involves collecting biological activated carbon, separating bacteria using domesticated culture medium comprising 0.l g beef extract, 0.2 g peptone, 0.l g sodium chloride, 0.005 g humic acid and 20 g agar, screening bacteria and evaluating degradation property of humic acid.
NOVELTY - Microbial composition comprises 16-25 wt.% photosynthetic bacteria, 13-20 wt.% lactic acid bacteria, 12-20 wt.% yeast, 5-10 wt.% Actinomycetes, 3-12 wt.% Acetobacter aceti, 15-26 wt.% sulfur reducing bacteria, 1-6 wt.% Bacillus and 1-6 wt.% Bifidobacterium.    USE - The microbial composition is used for sewage treatment (claimed).    ADVANTAGE - The composition enables simple operation of sewage treatment having high survival rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing the composition, which involves (a) dissolving 4-6 kg brown sugar in 80-120 kg purified water to obtain culture medium, (b) adding the culture medium to 3.4-6.4 kg microbial composition comprising 0.7-1.5 kg photosynthetic bacteria, 0.4-0.8 kg lactic acid bacteria, 0.7-1 kg yeast, 0.5-0.9 kg Actinomycetes, 0.3-0.5 kg Acetobacter aceti, 0.4-1 kg sulfur reducing bacteria, 0.2-0.3 kg Bacillus and 0.2-0.3 kg Bifidobacterium, (c) dissolving 0.4-0.6 kg urea, 180-220 g potassium dihydrogen phosphate and 40-60 g vitamin C in 5 l water, adding the dissolved mixture to the mixture obtained in step (b), mixing, sealing and incubating at 25-35 degrees C under illumination, and (d) shaking evenly for 2 times per day after 2 days, ventilating every half an hour, dissolving 50 g D-isoascorbic acid in water, adding to the medium on third day, shaking evenly, stopping illumination on fourth day and detecting pH value, where the pH should be less than 3.8.
NOVELTY - Method of using activated sludge, involves obtaining activated sludge, centrifuging or filtering the sludge to remove water, adding 1-4 times of nonionic surfactant extracting solvent, stirring or ultrasonically extracting for 0.5-2 hours, centrifuging or filtering to obtain enzyme extracting solution, adding ethanol or acetone to enzyme extracting solution, transferring to room temperature, centrifuging the mixture for 0.5-1 hour and collecting the precipitate.    USE - The method is useful for processing activated sludge (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - This utility model claims one kind of intensive rabbit fermenting bed facility, belonging to the poultry breeding technology field. A one intensive rabbit for fermentation bed, comprising two rows of set face to face rabbit's, each row of said rabbit cage composed of multiple laterally extending's, rabbit's said lower layer rabbit cage are provided with a excrement cleaning plate, wherein said two rows of rabbit's bottom layer rabbit cage under blocking fecal leakage plate's lower part are provided with a mesh,'s corresponding said mesh is provided with a groove, said two rows of rabbit cage's lower part is provided with a fermenting tank, said fermentation tank is provided with a fermenting bed pad material. This utility model claims one kind of intensive rabbit for fermentation bed, the ferment pad material in the fermentation pool's scattering to rabbit dung dirt's in the fermentation tank in-situ dissolve, using rabbit urine adjusting fermentation bed material's humidity, the water flushing excrement's, saves the water resource and saves the labour force.
NOVELTY - Extracting unsaponifiable substance from shea olein comprises (i) adding lower alcohol and catalyst into shea olein and performing transesterification to obtain transesterified product; and (ii) subjecting transesterified product to molecular distillation to obtain molecular distilled light phase and heavy phase rich in unsaponifiable substance.    USE - The molecular distilled light phase is useful in preparing biodiesel. The unsaponifiable substance composition is useful in preparing oil, medicine and cosmetics (all claimed).    ADVANTAGE - The method produces product in solid form with high purity and has long shelf life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an unsaponifiable substance composition, prepared by the above method.
NOVELTY - This utility model claims one kind of combined integrated deodorizing device, which is suitable for treating municipal sewage, industrial waste water treatment, malodorous gas's processing urban solid waste, garbage transfer station and industrial produced in the process of producing's. Liquid phase aeration reaction area is divided into, active filler bio-reacting area and active carbon adsorption area, the three to two gas distribution plate, upper distribution plate is provided with a gas-liquid flow through hole, placed above. One is opened with upper air inlet and provided with side wall's perforated outlet; the upper part is provided with biological filler in the active filler biological reaction area, upper filler attached with active microorganism, up the side wall's active carbon absorption region is provided with an air outlet, the gas after purifying the air's discharge of the liquid phase aeration reaction region of the side wall's upper part This utility model's combined integrated deodorizing device set said physical and chemical and biological treatment technology, the processing effect is good, small floor area, low investment and low operation cost, and has great application prospect's.
NOVELTY - The machine has a feeding device provided with a pre-heating device, a high temperature cracking device and a controller. The pre-heating device is provided with a driving device, a screw rod and a barrel. The screw rod is rotatably fixed in a material cylinder. A heating layer is arranged between pre-heating areas. The high temperature cracking device is provided with another driving device. A controller controls the feeding device, the pre-heating device and the cracking device. The driving devices are electrically connected to the controller. The heating layer is fixed with the controller.    USE - Rubbish thermal cracking machine.    ADVANTAGE - The machine has high leak tightness, better material heating effect and high working efficiency. The machine ensures environmental protection, avoids waste discharge and realizes continuous operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an operation of a rubbish thermal cracking machine.
NOVELTY - A one anaerobic sewage treatment facility, which is anaerobic pool's in the domestic sewage flow high efficiency and comprehensive utilization. Anaerobic tank is composed of a reaction chamber, marsh gas pipe, a sealing cover, a water outlet pipe, a tank temperature sensor, a temperature signal line, heater, heater pipe array plate, side chain-belt-type transfer conveyor, heater water inlet pipe, a slurry pumping port, a mud sink falling tank, a return pipe, a water inlet pipe. The separating wall between the bottom end's's anaerobic tank and pool bottom's space between the upper sealing cover and the pool's anaerobic tank left side wall and left side wall sealing cover's inner space is equipped with side chain-belt-type transfer conveyor, a machine body of a rotating carrier driven wheel, a chain transfer belt, transfer chain support guide wheel, the bearing wheel transfer and transferring the steering support guide wheel, driving wheel and transfer transfer steering bearing.
NOVELTY - A sludge is treated using microorganism by fluidized sludge, biological treatment, sludge dehydration and biological induction in which biological treatment is performed by adding Candida lipolytica Y-57 (CGMCCNo. 5790) into bioreactor, adding Pseudomonas putida P-101 (CGMCC No. 5801), aerating, drying oil-containing sludge to not greater than 2%, oily water content is not greater than 150 mg/L, skimmering floating oil by skimmer device for recycling, and placing fine sand into sludge dehydration step.    USE - Microorganism treatment for sludge (claimed).    ADVANTAGE - Process reduces oil content in sludge to 0.3%.
NOVELTY - The device has a sludge recovery inner cylinder body (1) connected between a sewage treatment tank and an inner wall of the inner cylinder body. A mud inlet (2) is utilized for sending sludge to the inner wall of the inner cylinder body. A sludge pump is arranged between the inner cylinder body and an outer cylinder body (3). The sludge pump is arranged in the sewage treatment tank. A side wall of the inner cylinder body is provided with a water leakage hole (11). The outer cylinder body is connected with a sewage recycling pipe and a waste water processing tank (31).    USE - Un-powered pure ecological recycling device for wasted metal sludge.    ADVANTAGE - The device utilizes heat to kill the bacteria and sludge from domestic sewage, and utilizes the non-toxic biodegradable organics and heavy metals safely for household or farm green fertilizing to material recycling purposes.    DESCRIPTION OF DRAWING(S) - The drawing shows a cutaway perspective view of an un-powered pure ecological recycling device for wasted metal sludge.    Sludge recovery inner cylinder body (1)    Mud inlet (2)    Outer cylinder body (3)    Water leakage hole (11)    Waste water processing tank (31)
NOVELTY - This utility model claims one kind of environment-friendly marsh gas tank, liquid outlet tube's chamber and comprising a tank body, a feeding pipe, an air outlet pipe and a tank body, between the leading to the sewage storage tank and acidification chamber leading to the marsh gas generating chamber are set between the filter wall, leading to the top of the tank body is provided with a feeding pipe and a liquid outlet pipe, the liquid outlet pipe and the biogas liquid's top of the hydraulic tank is connected with the outlet's sewage tank and feeding pipe are respectively connected with the acid chamber, an air outlet pipe is composed of marsh gas generating chamber by biogas liquid chamber and a hydraulic tank is composed of a tank body top; the marsh gas generating chamber's liquid is set in the grid-shaped arrangement's multiple layers, each layer of box between the clapboard, slag outlet is set on one side of acid chamber's. The marsh gas tank main body is designed to be three layers, increasing the gas pressure to generate the marsh gas generator's inner space is divided into multiple honeycomb-shaped net box, increases the dead angle area, greatly increased, the utility model can make the agricultural and industrial wastes and human and animal excreta in time, reduce the occupied, purifies the environment.
NOVELTY - The utility model claims one automatic shell-breaking marsh gas fermentation tank, the tank from up to down in turn is provided with a water pressure, air storage chamber, fermenting, water pressure between the fermentation chamber through the connecting pipe and is connected with the air storage chamber is connected with the tank body external's gas pipe, is connected with the fermentation tank body is inserted into's feeding pipe, the gas storage chamber is set with a # and several cone cylinder shell, bottom shell's cone cylinder is sharp and the fermentation chamber, the top end's shell breaking cylinder and the cone's base plate water pressure chamber is fixedly connected with the frontal and the tank body are fixedly connected. The utility model is provided with automatic breaking device in the fermentation tank, which not only can crush the shell layer floating slag, and it can soften, soaking the shell layer part of the scum re-depositing, digestion, improve the conversion rate of raw materials, reduces the slag, and the slag is easy.
NOVELTY - Method for preparing ammonia-oxidizing archaea bacteria enriched culture medium involves (a) preparing ammonia-oxidizing archaea bacteria enriched culture medium, (b) inoculating biological film or active sludge in the medium, (c) adding antibiotics to the medium, and (d) filtering the medium and repeating the step (c) for filtrate.    USE - The method is useful for preparing ammonia-oxidizing archaea bacteria enriched culture medium used for treating sewage system (claimed).    ADVANTAGE - The method enables to prepare ammonia-oxidizing archaea bacteria enriched culture medium which is pure and improves sewage processing biological denitrification ability.
NOVELTY - A Zoogloea resiniphila strain HJ1 (CCTCC M2012235) with o-xylene degradation ability, is new.    USE - The Z.resiniphila strain HJ1 is useful for degrading o-xylene in organic pollutants including benzene, toluene, ethylbenzene, xylene and chlorobenzene (all claimed), and converting o-xylene into carbon dioxide, water and cell biomass, and in degradation of benzene series pollutant.    ADVANTAGE - The Z.resiniphila strain HJ1, degrades o-xylene at a rate of 5.33 mg/l hour, and has strong resistance and maximum specific degradation rate of 0.19 mg o-xylene/mg cells hour.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of Z.resiniphila strain HJ1 in degradation of o-xylene in organic pollutants.
NOVELTY - Bacteria capable of degrading pentachlorophenol, are new. The bacteria are Citrobacter (CGMCC NO: 7817).    USE - The bacteria, preferably Citrobacter is useful for degrading chlorophenol compound, preferably pentachlorophenol in polluted water (all claimed).    ADVANTAGE - The bacteria has good adaptive capacity to environment, and tolerance to chlorophenol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the bacteria.
NOVELTY - Method for preparing self-circulating microorganism flocculant, involves screening flocculating microorganism from active sludge organic waste water treatment plant or other sludge, enriching culture, preparing strain suspension, culturing, inoculating flocculating microbial strain 25-37 degrees C and 120-180 rotations per minute (rpm) for 24-72 hours, sterilizing fermentation culture medium, and inoculating strain in organic waste water.    USE - The method is useful for preparing self-circulating microorganism flocculant used for organic matter waste water treatment in high organic waste water brewing industry, food processing industry, or pharmacy production (all claimed).    ADVANTAGE - The method is simple, cost-effective, and utilizes residual sludge.    DETAILED DESCRIPTION - Method for preparing self-circulating microorganism flocculant, involves screening flocculating microorganism from active sludge organic waste water treatment plant or other sludge, enriching culture, preparing strain suspension, culturing in beef extract peptone culture medium, potato culture medium, wort culture medium, or bean sprout juice culture medium, inoculating flocculating microbial strain 25-37 degrees C and 120-180 rotations per minute (rpm) for 24-72 hours, sterilizing fermentation culture medium, and inoculating strain in organic waste water.
NOVELTY - The method involves pre-treating the garbage using anaerobic fermentation biogas which is generated from food garbage. The biogas slurry is discharged for pre-treating the garbage. The pre-treated food and kitchen waste are discharged to methane post system. The pH value of mixture solution is adjusted for certain time using hydrogen chloride and sodium hydroxide to form high pure nitrogen gas.    USE - Method for processing solid waste in food garbage from kitchen for producing biogas such as hydrogen and methane.    ADVANTAGE - The energy consumption for producing hydrogen and methane can be reduced reliably. The production process of hydrogen and methane can be simplified, such that the production cost of hydrogen and methane can be reduced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the method for processing solid waste in food garbage from kitchen for producing biogas. (Drawing includes non-English language text)
NOVELTY - Rice straw is crushed, irradiated, treated with sodium hydroxide solution and reacted at 80-100 degrees C. The obtained mixture is filtered, washed, dried, and mixed with sodium acetate buffer solution. Cellulose is added to resultant mixture, maintained at constant temperature of 30-50 degrees C, and subjected to oscillating reaction at the speed of 120-140 r/minute for 72-96 hours to obtain fermentation liquid containing ethanol.    USE - Preparation of ethanol used as fuel.    ADVANTAGE - The method efficiently provides ethanol, with suppressed crystallinity of cellulose and improved conversion rate of degradation and saccharification efficiency, under mild reaction condition in short period of time with reduced consumption of energy without affecting the environmentally-friendly.    DETAILED DESCRIPTION - Rice straw is crushed to the size of 20-40 meshes, and irradiated. The mixed materials are treated with 0.3-0.7% sodium hydroxide solution in the solid-liquid ratio of 1:10-50, stirred uniformly, reacting at 80-100 degrees C for 0.5 hours, filtered, and washed into neutrality by water. The resultant material is placed in vacuum drying box at 50-70 degrees C for 24 hours, and obtained solid product is mixed with sodium acetate buffer solution in the solid-liquid ratio of 1:10-50. Cellulose (200-250 mu g) is added to the resultant mixture, and maintained at constant temperature of 30-50 degrees C. The obtained mixture is subjected to oscillating reaction at the speed of 120-140 r/minute for 72-96 hours to obtain fermentation liquid containing ethanol.
NOVELTY - Plant growth activator comprises 25-35 wt.% sulfur fermented extract (sic), 20-25 wt.% halophilous plant fermented extract, 20-25 wt.% herbal medicine fermented extract and 25-35 wt.% rice bran fermented extract.    USE - The composition is useful for promoting the growth of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the composition, which involves separately ripening and fermenting the above raw materials using effective microorganisms (EM) at room temperature, and mixing the obtained extracts.
NOVELTY - Invention relates to the field of agriculture, namely to viticulture. The method comprises initially single seeding in a row of vines on 3-year agro-technological cycles in inter-row spacing unsown in the previous cycle of winter triticale alternating in varieties cycles of selection of Krasnodar Research Institute of Agriculture n.a. Lukyanenko. Yearly in the cycles the green mass is trimmed at the stem elongation of plants in the spring. In the summer in the inter-row spacing soil the matured plant mass is embedded with ears of corn of triticale and agrobiological stimulant of effective microorganisms (EM) "Baikal EM-1" based on the special nutrient medium "EM syrup". At that together with the biomass of triticale and the stimulant EM in the inter-row spacing soil the organic matter of vegetable pulp (OP) is embedded at a rate of 380 kg/ha.    USE - Agriculture.    ADVANTAGE - Method enables to increase the natural fertility of the soil, vineyard productivity, to improve quality of grapes grown and vine-winemaking products through the creation of agro-technical conditions of increased growth and development of micro-organisms of the soil biota by increasing their biological activity due to the greater number of the organic matter in the treated soil.1 tbl, 1 ex
NOVELTY - An amido-amine compound (I), is new.    USE - As antimicrobial agents, surfactants (claimed), particularly cationic Gemini surfactants, emulsifiers, solubilizing agents, dispersing agents, foaming agents, and dispersing agents; used in compositions for fabric conditioning, detergent compositions, as washing agents, as adjuvants for agricultural active compounds and pharmaceutical active compounds; and also used in manufacturing cosmetics, shampoos, lotions, and personal care products.    ADVANTAGE - The amido-amine compounds have excellent surface activity; and are prepared by simple, economical and environmentally friendly process.    DETAILED DESCRIPTION - An amido-amine compound of formula (I), is new.    n=2-22C alkyl chain;    Y'=2-8C alkyl chain;    Q'=2-10C alkyl chain;    R1 and R2=1-5C lower alkyl groups;    X=F, Cl, Br and I.    INDEPENDENT CLAIMS are included for the following:    (1) preparing the compound (I); and    (2) an aqueous composition comprising the compound (I) dispersed in water or water-miscible solvent.
NOVELTY - Preparation (P1) of 2-((2-amino-6-oxo-1,6-dihydro-9H-purin-9-yl) methoxy)ethyl-N-((benzyloxy)carbonyl)-L-valinate containing not greater than 1 wt./wt.% of its D-isomeric impurity as determined by high-pressure liquid chromatography (HPLC), involves reacting 2-amino-1,9-dihydro-9-((2-hydroxyethoxy)methyl)-6H-purin-6-one (i.e. acyclovir) with carbobenzyloxy-L-valine at temperature of -20 degrees C to 20 degrees C.    USE - In the preparation of 2-((2-amino-6-oxo-1,6-dihydro-9H-purin-9-yl)methoxy)ethyl-N-((benzyloxy)carbonyl)-L-valinate which is used in making valacyclovir hydrochloride (claimed) for treating herpes simplex and varicella-zoster viral infections in humans.    ADVANTAGE - The method is simple, cost effective, eco-friendly, and reproducible; affords high yields and purity; produces 2-((2-amino-6-oxo-1,6-dihydro-9H-purin-9-yl) methoxy)ethyl-N-((benzyloxy)carbonyl)-L-valinate (II) containing not greater than 1 wt./wt.% of its D-isomeric impurity as determined by HPLC; produces valacyclovir hydrochloride having chiral purity greater than or equal to 99 wt./wt.% as determined by HPLC; and is well suited for commercial production.    DETAILED DESCRIPTION - Preparation (P1) of 2-((2-amino-6-oxo-1,6-dihydro-9H-purin-9-yl) methoxy)ethyl-N-((benzyloxy)carbonyl)-L-valinate of formula (II) containing not greater than 1 wt./wt.% of its D-isomeric impurity of formula (V) as determined by high-pressure liquid chromatography (HPLC), involves reacting 2-amino-1,9-dihydro-9-((2-hydroxyethoxy)methyl)-6H-purin-6-one of formula (III) (i.e. acyclovir) with carbobenzyloxy-L-valine of formula (IV) at temperature of -20 degrees C to 20 degrees C. An INDEPENDENT CLAIM is included for preparing (P2) valacyclovir hydrochloride (I) having chiral purity greater than or equal to 99 wt./wt.% as determined by HPLC, involving deprotecting the compound (II), converting valacyclovir into valacyclovir hydrochloride (I), and isolating valacyclovir hydrochloride (I).
NOVELTY - Nutrient soil comprises raw materials comprising 50-70 pts. wt. soil (new), 40-60 pts. wt. organic fertilizer, 0.5-2 pts. wt. acidic soil flora, 5-10 pts. wt. decomposing bacteria, 1.2-3 pts. wt. nitrogen fixing bacteria, 0.05-1 pts. wt. pH buffering agent, 3-10 pts. wt. bacterial cellulose, 2-5 pts. wt. curing agent, and pts. wt. 15-30 soil water retention agent.    USE - The nutrient soil is useful for Karst vegetation (claimed).    ADVANTAGE - The nutrient soil provides excellent soil condition for Karst vegetation, and solves rocky desertification area, and promotes virtuous cycle of Karst ecosystems.
NOVELTY - Soil conditioner comprises 60-70 wt. % of natural calcium sulfate, 20-30 wt.% of zeolite containing 1-5 wt.% of polymethyl methacrylate, 1-3 wt.% of a seaweed extract, 1-3 wt. % of functional material of Yucca, and 1-2 wt. % of powder mixture of microorganism agent sprayed on a compound powder.    USE - The soil conditioner is useful as an organic agricultural product for crop growth.    ADVANTAGE - The eco friendly soil conditioner exhibits improved nutrient holding absorption, and prevents the damage of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the soil conditioner comprising: introducing and mixing natural calcium sulfate, zeolite with polymethylmethacrylate, seaweed extract and yucca; stirring the raw materials to form a mixture; granulating the mixed powder by spraying a microorganism agent to form a mold; drying the granules with moldings; selecting the dried granules to the moldings; and selecting the granules for a package.
NOVELTY - The utility model claims a kind of all oxygen supplying system for garbage fermentation device, comprising a fermentation cylinder (2) is set in the fermentation cylinder (2) above the thermometer (1) is inserted into the fermentation cylinder (2) stirring paddle (5) is provided with a fermentation tank (2) and the lower half part is the fermentation cylinder (2) is divided into two through hole part (3) is inserted into the fermentation cylinder (2), the lower half part of the space (4), the hole on the baffle plate (3) is uniformly provided with multiple air inlet holes. Solves the problem that the current lack compare utility is provided with oxygen supplying system for garbage fermentation device.
NOVELTY - Improving utilization value of hybrid carbon four comprises carrying out cracked and selective hydrogenation reaction with vinyl acetylene, 1,3-butadiene and 1-butene, placing the product into an extractive distillation system, separating 1,3-butadiene and four-carbon fraction to obtain 1,3-butadiene product, mixing refinery carbon four into a hydrogenation isomerization reactor to obtain isomerized product, rectifying tower section in the isomerization reactor and then separating into a tower kettle, and carrying out disproportionation reaction with propylene and unreacted ethylene.    USE - The method is useful for improving utilization value of hybrid carbon four (claimed).    DETAILED DESCRIPTION - Improving utilization value of hybrid carbon four comprises carrying out cracked and selective hydrogenation reaction with vinyl acetylene, 1,3-butadiene and 1-butene, adding hydrogenation reaction product with content of less than 15x 10-9, placing the product into an extractive distillation system, separating 1,3-butadiene and four-carbon fraction to obtain 1,3-butadiene product, mixing refinery carbon four into a hydrogenation isomerization reactor to obtain isomerized product, rectifying tower section in the isomerization reactor and then separating into a tower kettle, carrying out disproportionation reaction with propylene and unreacted ethylene, placing four-carbon fraction through the hydrogenation reaction of hydrogenation to olefin content of less than 1%.
NOVELTY - Preparation of acyl azide compound, involves: taking the raw material comprising a carboxylic acid compound (I), carbonyl diimidazole as activating agent, sodium azide, lithium azide, tetrabutyl ammonium azide or trimethyl silicon azide as azide reagent, reacting the raw material with carboxylic acid in solvent at 10-80 degrees C for 1-10 minutes, adding azide reagent, continuously stirring for 1-3 hours, and obtaining acyl azide compound.    USE - For preparation of acyl azide compound (claimed) used as intermediate for preparing or synthesizing a compound to form isocyanate acetic acid.    ADVANTAGE - The preparation is cheap, does not need extra catalyst, has no pollution to the environment, has fast reaction speed, has simple post-treatment, yield is high, purity of the product is high, and the reaction condition is mild.    DETAILED DESCRIPTION - Preparation of acyl azide compound, involves: taking the raw material comprising carboxylic acid compound of formula RCOOH (I), carbonyl diimidazole as activating agent, sodium azide, lithium azide, tetrabutyl ammonium azide or trimethyl silicon azide as azide reagent, reacting the raw material with carboxylic acid in solvent at 10-80 degrees C for 1-10 minutes, adding azide reagent, continuously stirring for 1-3 hours, and obtaining acyl azide compound.    R=H, 1-20C alkyl, benzyl, optionally at least mono substituted phenyl, 1-adamantyl, 1-naphthyl, heteroaryl, substituted alkenyl or 3-coumarinyl.
NOVELTY - The method involves mixing and processing sludge and high concentration organic wastewater. The concentration of the volatile solid in high concentration organic wastewater is 120 g/L or greater. The metabolism process of microorganisms in sewage sludge is performed for separating the volatile solid in wastewater. The wastewater is steamed to the decomposition of the volatile solid due to generation of metabolic heat.    USE - Bio-evaporation method for zero-discharge treatment of highly concentrated organic wastewater in food factory, leather factory and chemical product factory.    ADVANTAGE - The metabolism process of microorganisms in sludge is performed for separating the volatile solid in wastewater so that the biodegradation property of volatile solid in the high concentration organic wastewater can be improved and the energy consumption for processing of the organic wastewater can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the Bio-evaporation method for zero-discharge treatment of highly concentrated organic wastewater.
NOVELTY - Device comprises a prewash tank, biological filter and an exhaust system sequentially connected. The prewash tank has a humidifying circulating system, a tail gas collecting chamber and an air inlet chamber. An inner part of the prewash tank has an inorganic filling layer. A filter material supporting layer made of fiber glass has a biological filter material with an environment temperature of 5-45 degrees C and comprising volcanic rock with a grain diameter of 15-50 mm. The spraying system is provided with a liquid distributor.    USE - Fertilizer fermentation workshop odor absorbing purifying device.    ADVANTAGE - The device is environment-friendly and does not generate secondary pollution. The device has high processing efficiency and better odor removing effect. The device has simple structure, convenient maintenance and high safety. The device saves the investment and maintenance cost.
NOVELTY - A zolpidem compound is prepared by carrying out condensation of aldehyde compound and aminopyridine compound in reaction solvent with presence of catalyst to obtain condensed imine compound, and subjecting imine compound in ring formation reaction with amide compound, catalyst, and additive to obtain N,N,6-trimethyl-2-(4-methylphenyl)-imidazo (1,2-a) naphthyridine-3-acetamide.    USE - Preparation of zolpidem compound (claimed).    ADVANTAGE - The preparation is short, controllable, and environment-friendly and has mild reaction condition, low cost, and high yield.    DETAILED DESCRIPTION - A zolpidem compound is prepared by carrying out condensation of aldehyde compound of formula (III) and aminopyridine compound of formula (II) in reaction solvent with presence of catalyst to obtain condensed imine compound of formula (V), and subjecting compound (V) in ring formation reaction with amide compound of formula (IV), catalyst, and additive to obtain N,N,6-trimethyl-2-(4-methylphenyl)-imidazo (1,2-a) naphthyridine-3-acetamide of formula (I).    R=N(CH3)2, N(n-Pr)2, OMe, ethoxy, tert.-butoxy, or benzyloxy.
NOVELTY - A water retention agent is prepared by subjecting 20-28 wt.% acrylic acid, 3-6 wt.% diammonium phosphate, 3-5 wt.% citric acid, 3-5 wt.% bentonite, 15-20 wt.% glutamic acid, 1.5-2 wt.% glycerol ethers, 3-5 wt.% hydrochloric acid, and 5-8 wt.% humic acid in reactor, performing polymerization reaction, adding ammonium persulfate salt, 2-2.5 wt.% sodium bisulfite, 2-2.5 wt.% methylene-bis-acrylamide, and 2-2.5 wt.% triethanolamine, heating at 60 degrees C for 2-3 hours under nitrogen protection, polymerizing, and curing.    USE - Preparation of water retention agent for soil.    ADVANTAGE - A water retention agent is environment-friendly and alkaline-resistant and has good physiological saline water performance and preparation process is low-cost, simple, safe, and reliable and has no pollution.    DETAILED DESCRIPTION - A water retention agent is prepared by subjecting 20-28 wt.% acrylic acid, 3-6 wt.% diammonium phosphate, 3-5 wt.% citric acid, 3-5 wt.% bentonite, 15-20 wt.% glutamic acid, 1.5-2 wt.% glycerol ethers, 3-5 wt.% hydrochloric acid, and 5-8 wt.% humic acid in reactor, performing polymerization reaction, adding ammonium persulfate salt, 2-2.5 wt.% sodium bisulfite, 2-2.5 wt.% methylene-bis-acrylamide, and 2-2.5 wt.% triethanolamine, heating at 60 degrees C for 2-3 hours under nitrogen protection, polymerizing, curing, adding mixture of nitrogen fertilizer and 18-28 wt.% phosphate fertilizer in citric acid, adding hydrochloric acid under presence of catalyst, subjecting components to granulator and mixing to obtain 50 mesh product.
NOVELTY - Preparation of 8-chlorotheophylline involves: (a) dissolving anhydrous theophylline in water, raising the temperature to 50-80 degrees C, dropping N-chlorosuccinimide to pH 6-7; (b) dissolving crude product in 5N sodium hydroxide aqueous solution, raising the temperature to 60-80 degrees C, when solids are completely dissolved, cooling to room temperature, adjusting pH of 3-3.5, separating the white solid, filtering, and washing by water to obtain 8-chlorotheophylline.    USE - For preparation of 8-chlorotheophylline (claimed) used as a medicine.    ADVANTAGE - The method obtains 8-chlorotheophylline having yield of 88-90%, HPLC purity of more than 99%; is green and environment-friendly; and reduce the cost and increases the utilization rate of the raw material.
NOVELTY - This new type utility claims one kind of compost turning machine roller, which is set with upper turning claw, a claw of a straight turning target earth claw and crushing claw, said turning claw is divided into two spiral line shape up the roller, and the target earth claw, claw corresponding to break at intervals, until a target earth claw is spade, a break claw is claw-shaped, this utility new type compost turning machine roller time in use is even, turning efficiency is high and it is not easy to compost the chunk.
NOVELTY - One for production of acidic oxidation potential water electrolyzer, mainly comprising an anode, a cathode and a water and salt raw material is composed of an aqueous electrolyte solution, wherein electrolyzer is tubular electrolyzer without membrane, the electrolyzer with a tubular anode, tubular cathode, an outer cathode tube, separating ring, an outer isolation ring, the electrode to the outside of the installation sequence is tube-type cathode, a tubular anode, an outer cathode tube, the tube is a plastic shell, a raw material is water, salt and phosphoric acid of an aqueous electrolyte solution, the electrolyte solution from the bottom of electrolyzer, and chemical reaction is combined by electrolysis in the electrolyzer from the electrolyzer upper part out of all acidic oxidation potential water. This utility new type of purpose of this utility model is to overcome the production acid oxidization potential water using membrane method box type electrolyzer limited by purified water or softened water, needs to be limited to produce by-product sodium hydroxide aqueous solution and with low energy consumption and high yield. The purpose is to avoid using non-diaphragm electrolyzer method of simultaneously electrolyzing hydrochloric acid and salt of the aqueous solution product in the presence of hydrochloric acid and chlorine-containing residue for biological and so on.
NOVELTY - This new type utility claims one marsh gas purifying system, comprising a biogas gas holder, a desulfurizing device, removing device, a methane gas cabinet through the desulfurizing tower of a desulfurization device connect with the said desulfurizing tower through the pre-cooler, a blower and a removing device of front separator tower connecting, in the said removing device, a tower front part lower filter separator through the front tower connecting with the absorption tower, absorption tower by a cooler, a separator gas buffer tank and the compressor rear connecting tower, a tower top connect with the regeneration tower, a regeneration tower middle part connecting the solution immersion, a boiling solution of the other end is connected with a regeneration tower bottom connecting the bottom of said regeneration tower through the barren solution pump is connected with a tower top connecting in a regeneration tower is provided with a pressure-reducing device and heating device. This utility new type the marsh gas purifying system, it has good economical efficiency and good effect of decarburization.
NOVELTY - Producing nano carbon and hydrogen comprises reacting raw materials with hydrocarbon at pressure of 0-1 MPa and temperature of 500-850 degrees C, catalytic cracking the hydrocarbon to obtain crude product of nano carbon and hydrogen, calcining the carbon nano-crude product at 250-400 degrees C for 0.8-1.5 hours, refluxing the crude product in concentrated hydrochloric acid for 2 hours, collecting the solid and then drying.    USE - The method is useful for producing nano carbon and hydrogen (claimed).    ADVANTAGE - The method is capable of economically producing the nano carbon and hydrogen with high purity.
NOVELTY - Biological fertilizer preparation involves utilizing (in wt.%): Ganoderma lucidum waste (67-70), animal manure (20-23), pond scum (9), biological species (1) and balanced amount of water.    USE - Method for preparing biological fertilizer (claimed).    ADVANTAGE - The method enables to prepare biological fertilizer in eco-friendly manner.
NOVELTY - Organic fertilizer comprises (in %): livestock manure (10.5), straw fiber (35), animal bone powder (10.5), tung seed cake (13.5), cellulose (3.15), neutral protease (6.3) and fermentation microbial inoculum (1.3).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is manufactured in simple and cost-effective manner, and ensures high effect without damaging soil in green and eco-friendly manner.
NOVELTY - Producing biological organic fertilizer involves mixing (in %): sugar filtered mud (46-49), chicken manure (22) cassava slag, (15-18), tong bran (8), wheat bran (4), brown sugar (1), biological strains (1) and water to obtain a mixture having water content of 55-60%. The mixture is fermented anaerobically, dried at low temperature to obtain water content of less than 5% and then crushed to obtain fertilizer powder of size 20-30 mesh. The obtained fertilizer is packed in bag.    USE - Method for producing biological organic fertilizer (claimed) used for recycling sugarcane mud waste.    ADVANTAGE - The method enables to produce biological organic fertilizer in cost effective-manner, and ensures good economic benefit and social benefit.
NOVELTY - Producing organic fertilizer involves collecting dry branches and fallen leaves of green plants of garden. The collected leaves and dried branches are cut, crushed and then mixed to obtain a mixture. Dairy manure and microbial inoculum are added to obtained mixture and then stirred and mixed uniformly. The mixture is fermented to decompose materials and obtain organic fertilizer with enhanced fertility.    USE - Method for producing organic fertilizer (claimed) used for improving physical and chemical properties of soil.    ADVANTAGE - The method enables to produce organic fertilizer in simple, cost-effective and eco-friendly manner, and ensures high nutrient content.
NOVELTY - Improving fermentation efficiency of microbial fertilizer involves decomposing organic matter at 70-80 degrees C, where microbial survival rate is more than 50%.    USE - Method for improving fermentation efficiency of microbial fertilizer (claimed).    ADVANTAGE - The method enables to improve fermentation efficiency of microbial fertilizer in less time and efficiently.
NOVELTY - Producing organic biofertilizer involves utilizing animal excrement and biological strain to obtain a mixture. The mixture is fermented, dried at low temperature and then crushed to obtain another mixture. The obtained mixture is granulated, measured and then packed.    USE - Method for producing organic biofertilizer (claimed).
NOVELTY - Manufacturing fertilizer involves mixing (in wt.%): biogas residue (60-80), monopotassium phosphate (6-12), calcium superphosphate (6-8), potassium chloride (5-10) and humic acid (3-10) to obtain fertilizer that is piled and applied to field.    USE - Method for manufacturing fertilizer (claimed) used for improving crop yield by improving soil fertility.    ADVANTAGE - The method enables to manufacture fertilizer in eco-friendly manner and ensure improved biogas utilization rate.
NOVELTY - Biological organic fertilizer comprises (wt.%): animal manure (15-20), crop straw (25-30), fly ash (15-25), rapeseed (20-25), Phellodendron leaves (3-6), biological enzyme (1-3) and organic fertilizer fermenting agent (1-3).    USE - Biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer has fly ash and rapeseed meal, which increase content of mineral in fertilizer provide nutrition content of fertilizer.
NOVELTY - Preparing 2,3-dichloropyridine, comprises reacting nicotinamide as raw material with sodium hypochlorite, distilling to remove water, extracting methylene chloride 3-aminopyridine with methylene chloride and recovering 3-amino pyridine with yield of more than 93%, reacting hydrogen peroxide containing 2-chloro-3-aminopyridine with hydrochloric acid solution to obtain 2-chlorine-3-amino pyridine with yield of more than 85%, and performing diazotization process to 2-chlorine-3-amino pyridine.    USE - The method is useful for preparing 2,3-dichloropyridine (claimed).    ADVANTAGE - The method is capable of preparing 2,3-dichloropyridine with less side reaction and high yield in a simple manner.
NOVELTY - Preparing lamotrigine, comprises reacting aminoguanidine bicarbonate with 2,3-dichlorobenzoyl cyanide under acidic conditions to produce 2-(2,3-dichlorophenyl)-2-(guanidinoimino) acetonitrile salt, neutralizing the product using alkali, heating 2-(2,3-dichlorophenyl)-2-(guanidinoimino) acetonitrile salt with organic solvent for cyclizing, adding active carbon into the crude product for decoloring and recrystallizing, washing the crystal, and drying in vacuum.    USE - The method is useful for preparing lamotrigine (claimed).    ADVANTAGE - The method is capable of preparing lamotrigine with high purity and high product yield in a mild, cost-effective and eco-friendly manner.
NOVELTY - An ammonia-containing mixed refrigerant contains 3-90 wt.% component 1 which is ammonia, 5-80 wt.% component 2 composed of ethane, propane, propylene, isobutane, butane, 1-butene, and/or isobutene, and 1-75 wt.% component 3 composed of trifluoroiodomethane, difluoromethane, 1,1-difluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,2,2,-tetrafluoroethane, 1,1,1,2,3,3,3-heptafluoropropane, trans-1,3,3,3-tetrafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, and/or 1,1,2,2,3-pentafluoropropane.    USE - Ammonia-containing mixed refrigerant for replacing pure ammonia refrigerant in small, medium, and large refrigeration system.    ADVANTAGE - The refrigerant has low toxicity and flammability, high safety, and good intersolubility, simplifies oil-separating system, reduces system cost, and improves system efficiency.
NOVELTY - Straw is cut using a guillotine, placed in a carbonization furnace, dehumidified, pyrolyzed at 300-400 degrees C to obtain pyrolytic carbon, and cooling formed charcoal.    USE - Continuous and quick carbonization of agricultural straw (claimed).    ADVANTAGE - The method carries out dehumidification before pyrolysis, which reduces energy consumption during pyrolysis as moisture-removal process is not required. Per ton of straw material (dry weight) provides 300-360 kg charcoal, 200-260 kg vinegar, 8-30 kg tar, and 600-750 m3 flammables.
NOVELTY - High calorific value non-polar biological oil/gasoline homogenous fuel is prepared by refining and primary upgrading biological oil in closed hydrogen atmosphere in presence of catalyst by catalytically cracking 380-420 degrees C for 30-50 minutes in which catalyst is nickel-cobalt-molybdenum loaded hydrogen exchange zeolite socony mobil (NiCoMo/HZSM-5), relieving pressure upon completion of catalytic cracking, filtering, decoloring by adsorption chromatography using silica gel, eluting out polar components, collecting non-polar components, combining, and vacuum removing mobile phase.    USE - Preparation of high calorific value non-polar biological oil/gasoline homogenous fuel for gasoline engine.    ADVANTAGE - The preparation of high calorific value non-polar biological oil/gasoline homogenous fuel is environment-friendly, improves smell and calorific value, and yields thermodynamically stable product.    DETAILED DESCRIPTION - High calorific value non-polar biological oil/gasoline homogenous fuel is prepared by refining and primary upgrading biological oil in closed hydrogen atmosphere in presence of catalyst by catalytically cracking 380-420 degrees C for 30-50 minutes in which catalyst is nickel-cobalt-molybdenum loaded hydrogen exchange zeolite socony mobil (NiCoMo/HZSM-5) where, nickel(II) ion (Ni2+), cobalt(II) ion (Co2+), and molybdenum(III) ion (Mo3+) with molar ratio of 1:1:0.5-1 and adding amount is 1-8%, relieving pressure upon completion of catalytic cracking, filtering, decoloring by adsorption chromatography using silica gel, ethyl acetate-petroleum ether mobile phase with volume ratio 1:1, and gas chromatography-mass spectrometry online tracking and monitoring, eluting out polar components, collecting non-polar components, combining, and vacuum removing ethyl acetate and petroleum ether.
NOVELTY - The method involves adding proper amount of water into a reaction kettle (1) to make natural phase separation of water and biological oil solid solution. An extraction coupling chemical conversion method is used in the aqueous solution of organic acid and aldehyde compound such as corresponding ester, acetal and hemiacetal by esterification or acetalation reaction so as to reduce bio-oil water content, acid value and improve a heat value in the biological oil, hot stability and combustion performance. Oil solution phase catalytic hydrodeoxygenation is carried out to prepare vehicle fuel oil.    USE - Split-phase biological oil extracting substance upgrading method.    ADVANTAGE - The method enables realizing upgrading process of oil water content and producing the high heat value and acid value.    DETAILED DESCRIPTION - The extracting agent and catalyst are added into a reaction kettle, where the extracting agent comprises benzene, toluene, dimethylbenzene, cyclohexane, ethyl acetate and butyl acetate. The catalyst comprises sulfuric acid, benzene sulfonic acid, or strong-acid cation exchange resin.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a split-phase biological oil extracting substance upgrading method.    Reaction kettle (1)    Condenser (2)    Mixing extracting slot (3)    Overflow port (10)    Standing settling tank (12)
NOVELTY - A dimethyl ether-containing biomass ethylene fuel contains 20-90% dimethyl ether, and 10-80% biomass ethylene.    USE - A dimethyl ether-containing biomass ethylene fuel (claimed).    ADVANTAGE - The dimethyl ether-containing biomass ethylene fuel is pollution-free, combusts safely, and has no residue and black smoke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of dimethyl ether-containing biomass ethylene fuel which involves using biomass ethylene raw material, ethanol, and composite acid catalyst, and subjecting to dehydration reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of dimethyl ether-containing biomass ethylene fuel preparing device.    1st tank (1)    2nd tank (2)    Mixed tank (3)    Check valve (4)    Pipeline (5)
NOVELTY - Integrated joint production of castor biodiesel and castor protein feed is performed by grinding castor bean, adding methanol and alkali catalyst, stirring to obtain castor oil and castor cake, separating castor biodiesel, drying castor cake, adding boiling water, and drying to obtain castor protein feed.    USE - Integrated joint production of castor biodiesel and castor protein feed (claimed).    ADVANTAGE - Production process increases added value of products. Products have high quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of an integrated joint production of castor biodiesel and castor protein feed. (Drawing includes non-English language text).
NOVELTY - A hogwash oil or waste oil pretreatment process is performed by selecting swill oil or waste oil as raw material, discharging into pool, adding acid solution, heating, mixing to sufficiently acidify raw material, letting to stand for precipitation with grease at upper layer, and sewage sludge in middle and lower layer, filtering oil to remove slag, adding concentrated acid, heating for acid digestion making large amounts of carbide polymer, precipitating impurities to obtain acidified oil, washing, dehydrating, and bleaching.    USE - A hogwash oil or waste oil pretreatment process for production of bio-diesel (claimed).    ADVANTAGE - Process can handle complex waste oil composition and obtained refined oil has uniform quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of waste oil pretreatment process. (Drawing includes non-English language text).
NOVELTY - The boiler has an upper boiler base (1) equipped with a dust hopper (2). A body (4) is provided with a hearth (6) that is provided with a flame bridge (13) and a feeding port (3). The body is provided with an air channel (12). The body is placed above a surface (5). The body and a cover (8) form a flue (11) connecting a chimney (10). The body is provided with a combustor (7). A burner is located in the hearth. The flue of the body is placed between ovens (9).    USE - Straw gasifying boiler for rural household.    ADVANTAGE - The boiler can be grazing using castoff of agriculture and forestry waste, straw and firewood and high temperature cracking and gasifying the rear combustion-supporting air with the combustion, and saves energy and reduces emission.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a straw gasifying boiler.    Upper boiler base (1)    Dust hopper (2)    Feeding port (3)    Boiler body (4)    Surface (5)    Hearth (6)    Combustor (7)    Cover (8)    Ovens (9)    Chimney (10)    Flue (11)    Air channel (12)    Flame bridge (13)
NOVELTY - The gauge has a pressure sensing element which is suspended in a septic tank (1). A marsh gas pressure gauge (5) is arranged on the periphery of a stainless steel cylinder (10). The upper portion of a stainless steel cylinder cover (11) is set with a groove. A screw (9) is inserted into the stainless steel cylinder cover groove. The stainless steel cylinder cover is exposed to the rear position of the stainless steel cylinder to maintain torsion seal such that the rainwater is not permeable in the stainless steel cylinder.    USE - Biogas pressure gauge of septic tank.    ADVANTAGE - The biogas information in the septic tank is transmitted to headquarter environmental protection agency through the mobile phone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Biogas pressure gauge of septic tank. (Drawing includes non-English language text)    Septic tank (1)    Marsh gas pressure gauge (5)    Screw (9)    Stainless steel cylinder (10)    Stainless steel cylinder cover (11)
NOVELTY - Preparation of catalytic biodiesel transesterification catalyst mixing magnesium nitrate and aluminum nitrate at mass ratio of 2.5-3.5 to obtain solution A, mixing potassium carbonate, potassium hydroxide, ammonium hydroxide, ammonium carbonate and sodium hydroxide or sodium carbonate to obtain solution B, mixing solutions A and B, crystallizing precipitates, centrifuging, washing and drying.    USE - Method for preparing catalytic biodiesel transesterification catalyst (claimed).    ADVANTAGE - The method is efficient, non-toxic, harmless and environmental-friendly.
NOVELTY - Preparation of catalytic nanomaterial biodiesel comprises mixing saturated solution of calcium chloride, oleic acid and petroleum ether to obtain solution A, stirring for 0.5-1 hours, adding ammonium carbonate dropwise, filtering and drying, dissolving ethanol and potassium carbonate to obtain solution B, stirring, mixing solutions A and B, reacting for 0.5-1 hour, filtering, drying, and roasting for 2.5 hours.    USE - Method for preparing catalytic nanomaterial biodiesel (claimed).    ADVANTAGE - The catalytic nanomaterial biodiesel is efficient, environmental-friendly and convenient for continuous operation.
NOVELTY - Production of environment-friendly plant organic fertilizer, involves: collecting garbage from social life and production, and classifying garbage into organic and inorganic substances; taking organic matter collection in fermentation tank, stirring in anaerobic fermentation strain, and fermenting for 6-8 hours; adding fermented organic garbage in drier, sterilizing, water cleaning all kinds of harmful substances, removing garbage organic species from water and drying at 110-150 degrees C for 2 hours; adding dried organic garbage into crusher and extruding crushed organic garbage.    USE - For production of environment-friendly plant organic fertilizer using garbage (claimed).    ADVANTAGE - The method turns waste into treasure, to achieve a comprehensive waste recycling and re-use of energy saving green economy. The product produced by the method has organic content above 40% and rich in micro fertilizer; has wide applicability for crops and also can be used for trees, flower and forest; can promote plant growth rate; and can reduce the plant food chain contamination.    DETAILED DESCRIPTION - Production of environment-friendly plant organic fertilizer using garbage, involves: (1) collecting garbage from social life and production, and classifying garbage into organic substance and inorganic substance; (2) taking the organic matter collection of the garbage in a fermentation tank, stirring in anaerobic fermentation strain fermentation, fermenting after fully stirring, fermenting for 6-8 hours; (3) adding the fermented organic garbage in drier, sterilizing, water cleaning all kinds of harmful substances, at the same time, removing garbage organic species from water and drying at 110-150 degrees C for 2 hours; (4) adding dried organic garbage into crusher for crushing expansion processing; and (5) extruding the crushed organic garbage into extrusion forming machine.
NOVELTY - The method involves reacting a compound of dechlorinating agent dissolved in N, N-dimethyl formamide to obtain dechlorinating agent in solution. Dechlorinating agent solution and oil mixing takes de-chlorination reaction. N, N-dimethyl formamide is separated after finishing reaction. Water soluble chlorine compound is added in residue. A water phase is separated to obtain dechlorinating. Oil is naphtha, petrol , diesel oil, coal oil, wax oil, crude oil or biomass. Mol ratio of chlorine is 0.3 to 5.0. Concentration of dechlorinating agent solution is 0.3 to 2.5mg/mL.    USE - Method for removing oil in chlorine-containing organic compound.    ADVANTAGE - The method enables effectively removing oil in chlorine-containing organic compound.
NOVELTY - A biodiesel is prepared by pretreating cottonseed oil, degumming, performing dephosphorization, adding acid and zirconium sulfate, mixing methanol, heating, stirring, refluxing, reacting, centrifuging, rotary evaporating, standing, soaking in sodium phosphate and magnesium oxide, mixing, rotary evaporating, heating, grinding, mixing methanol and cottonseed oil, adding catalyst, mixing, heating, stirring, reacting, removing catalyst, filtering, rotary evaporating, and recovering methanol.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method is simple and environment-friendly.    DETAILED DESCRIPTION - A biodiesel is prepared by pretreating cottonseed oil, degumming, performing dephosphorization, adding acid and 5 wt.% zirconium sulfate as catalyst, mixing methanol at molar ratio of 1:12, heating at 60 degrees C, stirring, refluxing for 2 hours, reacting, centrifuging, rotary evaporating to remove residual methanol, standing, soaking in sodium phosphate and magnesium oxide, mixing, rotary evaporating, heating at 80 degrees C for 12 hours, grinding to obtain sodium phosphate/magnesium oxide as base catalyst, mixing methanol and cottonseed oil at molar ratio of 10-15:1, adding 4-8 wt.% catalyst, mixing, heating at 67-75 degrees C, stirring, reacting for 2-3 hours, removing catalyst, filtering, rotary evaporating, and recovering methanol.
NOVELTY - Preparing a rubber grill charcoal comprises drying the rubber slag with 10-20% water, granulating the slag of the rubber and drying rubber slag particles, obtaining the rubber slag of particle, gasifying to obtain the biomass fuel gas, carbonizing, gasifying biomass fuel gas, drying rubber slag particles, distilling the rubber slag, cooling, crushing, and adding lime water to prepare roasted carbon.    USE - Method for preparing a rubber grill charcoal (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has controllable condition and low energy consumption.
NOVELTY - The system has a metal bottle whose end is connected with a gas outlet end using an exhaust valve to form a hydrogen gas flow channel, where the bottle is a single hydrogen storage bottle. A bottle outlet is provided with a manual pressure adjusting valve, a power supply system is provided with a DC/DC module, and a power supply management module is connected with a fuel cell stack, the bottle, an air inlet valve, an axial-flow fan, an exhaust valve, the DC/DC module, and a storage battery e.g. lithium ion battery.    USE - Portable proton exchange membrane battery e.g. lithium ion battery, lead-acid storage battery and super capacitor, power supply system (all claimed).    ADVANTAGE - The system has simple structure, compact and energy-saving, environment-friendly, and low operation cost. The system is convenient to carry, and has wide application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a portable proton exchange membrane battery power supply system. '(Drawing includes non-English language text)'
NOVELTY - Fuel cell power generation system comprises hydrolysis reactor water bath (1), hydrogen total pressure valve (2), hydrogen storage tank (3), hydrogen pressure regulator (4), hydrogen partial pressure valve (5), humidifier (6), water bath cooling system of a fuel cell (7), proton exchange membrane fuel cell (8), air compressor (9), water bath circulating water pump (10), water storage tank (11), hydrolysis reactor filter (12), hydrolysis reactor (13), magnesium hydride block (14) and air chamber (15).    USE - Fuel cell power generation system for hydrolyzing magnesium hydride for producing hydrogen (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell power generation system.    Hydrolysis reactor water bath (1)    Hydrogen total pressure valve (2)    Hydrogen storage tank (3)    Hydrogen pressure regulator (4)    Hydrogen partial pressure valve (5)    Humidifier (6)    Water bath cooling system of a fuel cell (7)    Proton exchange membrane fuel cell (8)    Air compressor (9)    Water bath circulating water pump (10)    Water storage tank (11)    Hydrolysis reactor filter (12)    Hydrolysis reactor (13)    Magnesium hydride block (14)    Air chamber (15)
NOVELTY - The tank has a tank body provided with a tank bottom foot. An end of the tank body is fixed with an end of a dropping liquid pipe. Another end of the dropping liquid pipe is connected with a dropping liquid collecting pipe. An upper part of the tank body is provided with an air inlet and an air outlet. An inner part of the tank body is provided with multiple upper division boards and lower division boards. The dropping liquid collecting pipe is provided with a liquid discharging valve and a blind plate. The air outlet is provided with a separation umbrella.    USE - Multi-stage horizontal separator tank.    ADVANTAGE - The tank adopts multiple separation principles so as to improve hydrogen purity of water electrolysis to produce hydrogen and oxygen mixture and utilizes spray separating plate dissolved oxygen that is separated from liquid due to diffusion effect. The tank utilizes a baffle plate so as to change flowing direction of the liquid and performs condensation operation of micro liquid drop so as to obtain pure gas from the air outlet. The tank has high air amount and air purity and better separation effect, and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multi-stage horizontal separator tank.
NOVELTY - Wastewater is treated by introducing wastewater to membrane separator, and to anaerobic reactor under sealed environment to provide controlled anaerobic operation, stirring anaerobic sludge, adding water, mixing to form micro-bubbles colliding with each other and producing turbulence and bubble coalescence, separating water from sludge, introducing to membrane separator containing hollow fiber membranes, purifying by pumping negative pressure, and feeding excess water to anaerobic reactor to maintain sludge concentration.    USE - Treatment of wastewater (claimed).    ADVANTAGE - The bioreactor improves mass transfer rate, accelerates treatment process, enhances separating efficiency of sludge and gas, and solves problems encountered in triple-phase systems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic membrane bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the anaerobic membrane bioreactor.    Inlet (1)    Membrane separator (2)    Hollow fiber membrane (3)    Anaerobic reactor (4)    Gas turbine (5)    Seal (6)    Exhaust port (7)    Drain (8)
NOVELTY - Poultry manure mixer comprises machine frame (1), speed reducer (2), transmission parts (3), stirring tooth (4), cover (5), universal wheel (6), handle (7), stirring shaft (8) and a motor (9), where the stirring shaft of bearing is installed on the machine frame. The other end of stirring shaft is fixed on stirring teeth, where stirring teeth of the stirring shaft is extended up to the side frame.    USE - Poultry manure mixer.    ADVANTAGE - The poultry manure mixer improves uniformity and ripening rate of poultry excrement, has good fermentation effect and higher fertilizer effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a poultry manure mixer.    Machine frame (1)    Speed reducer (2)    Transmission parts (3)    Stirring tooth (4)    Cover (5)    Universal wheel (6)    Handle (7)    Stirring shaft (8)    Motor (9)
NOVELTY - Preparation of a bimetallic biodiesel solid alkali catalyst comprises synthesizing calcium iron binary hydrotalcite catalyst; adding activator and distilled water, uniformly stirring to obtain a slurry mixture, where the activator is kaolin, montmorillonite, or sepiolite, where the weight ratio of hydrotalcite and the activator is (2-4):1; drying the slurry mixture at 95-120 degrees C; and crushing, and grinding.    USE - Method for the preparation of a bimetallic biodiesel solid alkali catalyst (claimed).    ADVANTAGE - The method has a conversion rate of more than 90%, has a low temperature activating treatment, and has a reduced energy consumption.
NOVELTY - Esterification catalyst for reducing acid of high acid value pepper seed oil, which is obtained by intercalation reaction of sulfuric acid and 50-mesh natural expandable graphite flake under the action of the potassium permanganate as oxidizing agent, where heterogeneous catalyst having the A, B, C of the three components, the component A incudes 50-mesh natural expandable graphite flake, the component B incudes potassium permanganate, and the C incudes concentrated sulfuric acid, where ratio of A:B:C is 1 g:0.05-0.10 g:2-7 ml.    USE - As esterification catalyst for reducing acid of high acid value pepper seed oil (claimed) for production of biodiesel.    ADVANTAGE - The catalyst is green and environment friendly; has high catalytic activity; provides short reaction time and high yield; avoids corrosion of equipment; reduces pollution; is easy for separation and regeneration; and reduces emissions and waste disposal costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for esterification and deacidification of high acid value pepper oil involving degumming and bleaching pepper oil, heating treated pepper oil; mixing methanol and treated pepper oil at molar ratio of 30:1 and heating at 60 degrees C; adding 8-12 wt.% the esterification catalyst; reacting for 2-3 hours; transferring reaction mixture to a separating funnel for overnight, transferring the methanol aqueous upper phase to a rotary evaporator and recovering the methanol, separating lower oil phase, drying to obtain deacidified pepper oil.
NOVELTY - This new type utility claims one kind of thymol of continuous synthesis device, comprising a gas raw material tank, a liquid raw material bottle and a pipeline reactor, the liquid raw material through the feed end of pipeline reactor is connected with the pipeline, a pipeline reactor through a bracket support, a pipeline reactor according to front and back is divided into heating section, heating section and a natural cooling section, gas raw material tank through pipeline is connected with the middle part of heat-conducting oil heating section, the lower part of the heating section is provided with a guide hot oil heater, an electric heating section of outer wall of the pipeline is provided with an electric heating wire, naturally cooling and discharging end of the valve section and the bottle connecting, the utility model is new type device used are non-pressure device, safety and reliable, the whole process is continuous production, saves energy, improves the yield and production cost decreasing.
NOVELTY - This utility new type relates to one kind of camphor production device, especially one-like camphor production device, wherein, comprising a one-time vaporizing kettle orderly connecting of the fractionating tower, second-time vaporizing kettle, a condenser and scraper, wherein the scraper is set up with a freezing water inlet and freezing water outlet, which is provided with cooling channels, and the material tray of scraper is located in cooling channel. The scraper into the production process so that the sheet-like camphor production of continuous smooth, there is no need, it saves time and labour, and the cooling performance can be immediately rear blade, it will not waste material, which can ensure the sheet of camphor, such as chroma, good viscosity, the purity is high and so on.
NOVELTY - One in urea production device of hot source recycling device, comprising a hydrolysis heat exchanger (4), heat exchanger (5), a reflux condenser (1), the hydrolysis tower (3), the analyzing tower (2), and the device are correspondingly connect with each other through the pipeline, a desorbing tower (2) comprises a first analyzing tower (21) and the second analyzing tower (22), wherein said hydrolysis tower (3) of the second outlet (33) is connected with one section decomposition heater (7) of heat exchange is connected with the inlet of the said one section decomposition heater (7) of heat exchange outlet hydrolysis heat exchanger (4) of heat exchange is connected with the inlet, and a hydrolysis exchanger (4) of heat exchanger outlet is connected with the second analyzing tower (22) of first inlet (2f). The advantages of this design, in the hydrolyzing tower out of waste heat in gas-liquid heating to up one section of decomposition heater heating of liquid, at the same time, the analyzing tower in gas-liquid heat application from one evaporation section hot heating device of liquid, so as to improve the utilization rate of hot source.
NOVELTY - This new type utility claims one crop straw carbonizing device, wherein it is mainly composed of carbonization cylinder (1), a carbonizing tank (1) upper are respectively provided with a feeding port, an exhaust pipe (2) and a carbon outlet. This utility new type not only has simple structure, but also has low cost, but also can treat local crop straw, so it is suitable to popularize and use.
NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace, comprising a machine frame, a furnace body, a feeding device, a combustion device, a stirring and ash falling device, the feeding device is set with a feeding device corresponding to the connecting port of the top of the furnace body, the top of the furnace body, a furnace body of the position close to the top part is provided with a fuel gas outlet, the combustion-supporting device is set on the upper furnace body, and an ash stirring device is set at the bottom of the furnace, this utility new type ash dropping device stirring raw material discharge carbon particles, can prevent the stack of fuel in the furnace is high, the device can be stable, effective of working, and preparing and of a gas, and the discharge carbon particles in the process, which effectively solves the fuel particles produce slag in the solar high temperature and static problem of this utility new type rear raw material gas remaining of carbon particles are carbon particles, the biomass particle for preparing the high efficiency of gas and carbon particles, improve the fuel utilization rate, more energy-saving and environment-friendly.
NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace and an ash stirring device, comprising a mortar, an ash disc, the ash turntable, the rotating shaft of the stirring head, a stirring motor, a dust plate set on the upper rotating shaft, the upper ash tray is provided with a plurality of dust area, upper of each ash falling area is provided with a plurality of dust between the dust along a plurality of uniformly distributed along the circumferential direction, respectively forming the ash part two adjacent ash falling area, the ash plate upper end upper face is provided with the ash groove hole, upper surface of ash plate is propped against end near the lower end face of blocking ash part stirring rolling effect of stirring head is capable of stirring and ash, can accelerate the material ash in an ash hole, entering into dust efficiency and effectively solves the raw material particles will produce the problem of slag in the high temperature, the utility model is new type alternatively taking ash and gas action, the action gas to the furnace body and the mortar sealing to prevent the combustion process and an ash process are the influence of combustible gas.
NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace feeding device, comprising a furnace cover, a furnace cover plate is set up with a feed inlet, a furnace cover plate at the bottom of the feed inlet position of two inclined side is provided with a guide plate, guide plate of the upper are respectively extended with a side baffle plate, a material guide plate of upper end edge extends upwards to form with upper baffle plate, side baffle plate and upper end of upper baffle plate tightly set on the oven cover, three surface of the guide plate of the bottom of the furnace cover to reduce flame skewered upwards, feed device capable of preventing heating caused by the material deformation such that the feeding action and part of service life, and a feeding mechanism feeding new fuel in the furnace, the new fuel guide is placed in the furnace fixing one angle, so that fire in the furnace will not produce broken discontinuous of continuous condition to prevent the gas supply of the expiration.
NOVELTY - This utility new type relates to biomass energy device technology field, especially relates to biomass reaction furnace combustion-supporting device, comprising a gas supply device, a gas pipe, a blowing joint, a plurality of combustion-supporting air pipe, two ends of the air pipe are respectively connect with the air supply device, a blowing joint, one end of the combustion-supporting air pipe are respectively connect upper of the blowing joint and joint is connected with the air blowing, combustion-supporting air pipe is provided with a plurality of holes, the biomass fuel is combustion-supporting air pipe, an air supply device supplying air as combustion improver, blowing joint through the gas conveying pipe, and a plurality of combustion-supporting air blowing pipe of blowing hole downwards uniformly blown up biomass fuel, a plurality of combustion-supporting air pipe blowing hole blowing uniform and combustion-supporting air pipe blowing the biomass fuel and material ash stay in the furnace to prevent the ash material gas together with , combustion-supporting effect is good, and it can control the air amount, which is convenient to adjust and control the temperature in the furnace.
NOVELTY - A one machine-made charcoal powder raw material screening device, referring to wood processing device field, comprising a machine frame of one up to the ground, is set up on the filtering roller of a machine frame, a filtering roller comprises a screening layer of first and second screening is located outside of layer, the outlet of a first screening layer is screening the end part of roller, and is provided with one bearing groove material outlet of the first screening layer, the outlet of said second screening layer is located in the middle at the bottom of filtering roller is provided with a discharging passage below the outlet of the second screening layer, the lower part of the conveying belt is provided with a discharging channel. This utility new type has simple structure, reasonable design, for the screening process, improves the sieving effect to ensure the screening process will not be material.
NOVELTY - A one machine-made charcoal powder raw material screening machine transmission mechanism, referring to wood processing device field, comprising one frame, upper filtering roller of the said machine frame, the circumference of said filtering roller of upper end fixing with one belt pulley is provided with one servo motor at the bottom of the said machine frame, output end of servo motor through a belt connecting said servo motor to the upper part of a continuously variable transmission, a continuously variable transmission of output end connecting with a first belt pulley, a first belt pulley through a belt connecting the pulley of filtering roller of upper end to drive the filtering roller to rotate. This utility new type has simple structure, reasonable design, using vertical design, is convenient to install, the rotating speed is easy to control, can screen material of different variety, good practicability, simple operation and maintenance.
NOVELTY - A machine-made charcoal powder feeding one emergency raking mechanism, referring to wood processing device technology field, comprising a set on the ground following one of a feed hopper, said feed hopper outlet at the bottom of the lower part is equipped with a conveying belt, a feed hopper is vertically provided with the front part for blocking material of one baffle plate, said upper baffle is provided with one through hole, which can prevent the material, a feeding hopper side is provided with one motor, one output end of said motor connecting with a speed reducer, the output end of said speed reducer connecting with a rotating shaft, said upper rotating shaft fixing a scraping the material spade, a scraping shovel the material feeding hopper, produce accumulation time when the material of the feeding hopper, starting the motor working, the motor drives the rotating shaft to rotate, so as to drive the scraper shovel working material, the material in the hopper of upper conveyer belt can solve the blocked material.
NOVELTY - A hydrogen generator, one output end of three-phase power, a rectifying circuit with the switch power source comprises a hydrogen generating device and controller, the controller comprising: a rectifying circuit are respectively connected with the input end of the power supply connecting of are respectively connected with the direct current switch circuit and an intelligent program control unit input end, output end of the intelligent program control unit through the direct current switch circuit and the hydrogen generating device, the hydrogen generating device set up of current signal, the temperature signal and the pressure signal to the intelligent program control unit; a hydrogen generating device comprises an electrolytic groove and cooling system, the two side of the electrolytic tank are respectively provided with a heat exchanger, is provided with a circulating cooling water inlet and outlet of the upper heat exchanger, inlet and outlet through the pipeline and the water pump is connected with the cooling system to form a circulation cooling system, the electrolytic tank of the heat exchanger upper part is provided with hydrogen and oxygen gas outlet. This utility new type is the electrolytic bath of the cooling system are organically combined, which changes the common direct current power supply in the electric control.
NOVELTY - This utility new type relates to one kind of oxygen/hydrogen mixed gas generator of water electrolysis tank structure, comprising one water main body, the main body is provided with water containing electrolyte of containing space and is equipped with several electrode plates, the two ends of the water electrolytic cell of main body are respectively provided with electrolyte inlet and electrolyte outlet, each electrode plate are continuous " Z electrode connecting part bent-shaped, and the upper end corner of each electrode plate are provided with bending of the set and the electrode terminal of said water side surface connecting two ends of the main body, a water body of two inner side surface are respectively provided with multiple electrode plate locating groove. This utility new type oxygen in hydrogen electrode plate of gas generator is in continuous N-shaped bent, the electrode plate greatly increases the contact area of the electrolyte, oxygen generating amount of hydrogen mixed gas is greatly increased.
NOVELTY - Utilization of pig manure in biogas system includes soaking fresh pig manure and piggery wastewater in storage pool (1) for 0.5-1 day, transferring through cutting pump (5) to anaerobic methane fermentation reactor (6), producing biogas, separating biogas residue using screw extruder (7), entering to reactor tank (8), transferring through lifting pump (10) to anaerobic sludge bed reactor (11), transferring through high pressure pump (12) to storage pool (1), drying biogas, entering desulfurizer (13), storing in flexible gas tank (14) and transferring to biogas user unit (15).    USE - Biogas system recycling and utilizing pig manure used for preparing biogas (claimed).    ADVANTAGE - The method shows 20-30% improvement.    DETAILED DESCRIPTION - Utilization of pig manure in biogas system comprises soaking fresh pig manure and piggery wastewater in storage pool for 0.5-1 day, transferring through pump to regulating pool, mixing using stirrer, transferring through cutting pump to anaerobic methane fermentation reactor, producing biogas, separating biogas residue using screw extruder, entering to reactor tank and into adjusting tank, transferring through lifting pump to anaerobic sludge bed reactor, transferring through high pressure pump to storage pool, drying biogas, entering desulfurizer, storing in flexible gas tank and transferring to biogas user unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of utilization of pig manure in biogas system.    Storage pool (1)    Cutting pump (5)    Anaerobic methane fermentation reactor (6)    Screw extruder (7)    Reactor tank (8)    Lifting pump (10)    Anaerobic sludge bed reactor (11)    High pressure pump (12)    Desulfurizer (13)    Flexible gas tank (14)    Biogas user unit (15)
NOVELTY - Method for preparing organic fertilizer, involves using raw materials comprising humic acid, nitrogen, phosphorus, and potassium. The method does not include step of heating and fermentation.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method does not include step of heating and fermentation. The organic fertilizer prepared by the method is superior to existing fertilizer, as it has excellent stability.
NOVELTY - Green biological organic fertilizer comprises animal excrement, plant straw, microbial fermentation complexing agent, Chinese herbal medicinal mixture, medical stone and lees.    USE - Green biological organic fertilizer.    ADVANTAGE - The fertilizer does not produce environment pollution, is simple to prepare and low cost, and prevents crop diseases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising adjusting water content of plant straw to 20-30 wt.%, crushing to 40 mesh, adjusting water content of animal excrement to 60-70 wt.%, drying Chinese herbal medicinal mixture, crushing to 40 mesh, mixing plant straw, animal excrement, Chinese herbal medicinal mixture and medical stone, uniformly mixing, piling to form open stack, controlling temperature to 15-30 degrees C; adjusting water content to 55-65 wt.%, adding microorganism fermentation complexing agent, performing open aerobic fermentation for 25-40 days, adjusting water content to 25-30 wt.%, sieving, uniformly stirring, feeding to roller drier, drying at 60-120 degrees C, cooling to obtain organic fertilizer having a water content of 5-20 wt.%.
NOVELTY - The fluidized bed coating machine has a main structure that is provided with an air circulation system (3) and a dehumidification device, and set on the fully closed portion of fluidized drying tower (1). The dehumidification device is provided with large particle drying agent for the fluidized drying tower. The drying tower is connected with the coating machine tower (5) by draft fan of air circulation system and heater (4) to realize fully enclosed air circulation.    USE - Fluidized bed coating machine used for preparation of water-based polymer coated fertilizer (claimed).    ADVANTAGE - The environment friendly coating machine can greatly reduce the labor consumption, improve the reproducibility of the coating process, save energy, satisfy technical requirement of large scale coating industry, and widen the application range of coating material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of water-based polymer coated fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fluidized bed coating machine used for preparation of water-based polymer coated fertilizer.    Fluidized drying tower (1)    Air circulation system (3)    Heater (4)    Coating machine tower (5)
NOVELTY - Absorption system comprises a compressor, a pre-processing unit, a refinery dry gas cooling unit, an absorption unit and a rectification unit. Separating tank material inlet is connected with gas-liquid phase. Absorption unit comprises a gas liquid separating tank, an absorbing tower and a methane denuding tower. The rectifying unit comprises a decarburization tower (17) and ethylene rectification tower. The carbon absorption tower (13) upper part is provided with a absorbent (20), where inlet and lower parts are provided with dry gas obtained from oil refinery (11).    USE - System used for recycling dry gas obtained from oil refinery (claimed).    ADVANTAGE - The absorption system enables to produce product that has high purity and recovery rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing absorption system, which involves:    (A) compressing and pre-processing, and cooling dry gas from oil refinery process to separate gas-liquid phase;    (B) entering gas phase into second absorption tower, and mixed with absorbent;    (C) taking carbodiimide, and separating gas liquid phase in a gas-liquid separating tank to obtain liquid phase;    (D) entering the obtained liquid phase in a methane converting desorption tower, where top part of denuding tower contains methane and air with dry gas obtained from oil refinery;    (E) cooling a rectifying methane comprises carbodiimide and absorbing agent in the second tower;    (F) separating carbodiimide and absorbent;    (G) rectifying the separated mixture of carbodiimide in the ethylene rectification tower to obtain product ethylene and ethane product; and    (H) recycling absorbent carbon in the second absorption tower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of absorption system.    Dry gas from oil refinery (11)    Carbon absorption tower (13)    Decarburization tower (17)    Absorbent (20)    Ethane product (22)
NOVELTY - 4-Hydroxycoumarin, co-aldehyde and pyridine-bromoacetophenone salt are dissolved in a solvent. An alkali as catalyst is added to mixture and reacted at 25-150 degrees C, to obtain 2-benzoyl-2H-furo(3,2-c)coumarin derivative.    USE - Synthesis of 2-benzoyl-2H-furo(3,2-c)coumarin derivative (claimed).    ADVANTAGE - The 2-benzoyl-2H-furo(3,2-c)coumarin derivative having high selectivity is economically and efficiently synthesized under mild reaction conditions within short period of time and with reduced energy consumption, with high yield and without environmental pollution.
NOVELTY - This utility new type provides one kind of preparation methanol water vapour reforming hydrogen of device for boiler, belonging to the field of chemical device field. Its technical solution is as follows: one kind of methanol water vapour reforming preparation for boiler device of hydrogen, comprising a boiler, a chimney, and connecting the tail flue of boiler and chimney, wherein the upper tail flue is provided with a smoke gas bypass connected in parallel, a flue gas bypass up is provided with a methanol cracking reactor, a methanol cracking reactor outlet through the heat exchanger of the boiler burner connecting. This utility new type of beneficial effect are: the utinity device, hydrogen-containing gas preparation, it can replace fuel oil, natural gas, heavy oil, coal and so on fuel boiler solves the pollution problem, using energy from self-use fuel boiler, waste heat of the fuel can effectively used, but also can realize generating gas is used for burning, substituted natural gas, reduce the cost, reduce the energy consumption, is caused by the production effect.
NOVELTY - This utility new type for fermenting bed cultivation technology of environment control system, comprising a pad groove type dumper bacterial liquid spray device, a negative pressure aeration and deodorization device, the fermentation bed space ventilation system, detect device and control system, groove type dumper bacterial liquid spray device, the action of negative pressure aeration device and deodorizing device, the fermentation bed space ventilation system and detect are controlled by the control system. This utility new type cultivation whole environment assumed from, in order to realize the purpose of benefit for cultivation, live stock excrement processing means, compost fermentation, environment-friendly and environment to detect in situ technical means such as, at the same time is comfortable living environment of building, to lowest of cost, realizes zero water of livestock waste processing, zero exhaust and zero pollution, groove type turning one cushion groove in the rear livestock excrement by turning the cushion groove type trolley stacking the participator one cushion groove working to effectively use device and reduce the cost.
NOVELTY - This new type utility claims one kind of domestic sewage factory sludge added of compound fertilizer production device, comprising a stirring tank, a concentrating and dehydrating machine, stirring mill, a fermenting tank, a crusher, a roller type sieve, first mixer, a drying machine, a second mixer and granulator, wherein the stirring tank and concentrating and dehydrating machine connecting, comprising a conveyer belt connecting concentrating and dehydrating machine outlet is connected with stirring mill inlet, crushing and stirring the fermenting tank connecting, drum-type electric sieve outlet is connected with first connecting stirrer, the outlet of first mixer and dryer inlet connecting, a dryer outlet connecting with a second mixer, the outlet of the second mixer connect machine, the invention has the following advantages: greatly reduces sludge treatment cost of, and it will not produce second pollution, and make it into organic inorganic compound fertilizer, capable of activating soil. compaction, promote growth and development, which is good.
NOVELTY - This new type utility claims one horizontal-type by using biomass fuel for continuously preparing combustible gas of device, comprising a shell, wherein the shell is column-shaped, transverse, upper side of the shell and the connecting chamber, upper end of storage chamber connecting with the feeding hopper, a shell of right end in is provided with a combustion head, right end is provided with an air inlet and a waste outlet, a shell of the left end in order of from left to right is punching piston and pushing piston, wherein the punching piston is provided with a plurality of transversely set up of , one end of the connecting rod of the punching piston connecting, and the other end can pass through the upper pushing piston, a piston, a pushing piston is provided with a vent hole, the piston and the second hydraulic cylinder connecting the pushing piston and the first hydraulic pressure jar connect, the left end of shell is provided with exhaust of gas outlet. This utility new type is simple in structure, low in cost, capable of efficiently and continuously preparing combustible gas and raw material is selected for material is low, sufficient combustion, for the environment is small, and high conversion rate.
NOVELTY - One biomass pyrolysis and high temperature flue gas comprehensive utilization system, the upper part and the hot cyclone separating machine carrier connect, hot carrier cyclone separating machine with the pyrolysis reactor connecting solid outlet, a flue gas through vacuum tube exchanger of hot source flow and air pre-heater of hot source flow connect, an air pre-heater hot source outlet of the biomass pre-dryer connecting of biomass pre-drier ceiling connecting biomass storage bin, the upper part through the lower part of fan and the regenerator connecting the lower part with the pyrolysis reactor connecting, pyrolysis reactor lower part of the multi-stage system is respectively connected with the regenerator, semi-coke discharging device and fractionating tower connecting. This utility new type can realize comprehensive utilization of flue gas in biomass pyrolysis process in pre-heating biomass raw material gasification and coking process, a fan hot carrier damage and melting the coking problem, vacuum tube exchanger and absorbed air pre-heater of heat entering into waste heat boiler, increases the energy utilization rate.
NOVELTY - This new type utility claims one kind of straw gasification furnace, the structure is as follows: the bottom part of gas cylinder is provided with a net-shaped, net-shaped furnace bottom part is equipped with oil-water separation chamber, a gas cylinder is provided with the ash outlet, the inner wall of gas cylinder is provided with a fuel gas pipe I, a gas pipe I of upper end is provided with an opening I and the lower end is provided with an opening II, a gas cylinder opening of II is provided with a fuel gas outlet II, the inner gas cylinder gas pipe I in part of is provided with a fuel gas outlet I, a gas pipe II one end of the gas outlet II connect, the other end connecting with the gas stove, gas pipe I at the bottom connecting oil pipe, the oil pipe is net-shaped furnace bottom and oil-water separation chamber, the opening direction of the tar pipe outlet is upward, and the outlet of the tar pipe is higher than the tar pipe; the blower through air channel automatic switch connecting lighting-up tuyere, the connecting air channel. This utility new type of straw gasification furnace saves fuel, discharge, an indoor smoke, tar-free and so on, capable of continuous 20 to 30 hours of human look after.
NOVELTY - This utility new type provides the biomass fuel gas generator dry ash outlet device and biomass fuel gas generator, wherein, biomass fuel gas generator type, comprising a collector, a seal device and cooling system. Wherein the cooling system comprises a cooling water tower and the water tank, a collector is supported on the water tank in, a cooling water tower is supported on inner surface of collector on the bottom of cooling water tower is provided with a water inlet, the top part of the cooling water tower is provided with a water outlet, the bottom port connecting collector of feeding port of sealing. Producer in produce of high temperature furnace ash by a cooling water tower, a collector and sealed conveyor surface contact type cooling for three times, the temperature of furnace dust of high temperature and maintain drying of status, reuse of; the whole ash discharging device can maintain seal status in the process of in the ash to avoid gas leakage or air from the device entering into the ash in furnace.
NOVELTY - This utility new type relates to one preparing biomass combustible gas of device, belonging to the field of energy chemical technology field. Device main body is a molten salt reactor, the top end is provided with a gas outlet, is provided with molten salt outlet and gasification gas inlet, a screen is provided with a porosity of less than 0.02 (mu) m molten salt reactor separating screen, molten salt reactor is further equipped with a feeding device, a molten salt reaction separating screen is horizontally installed between the molten salt reactor gas outlet distance of 1/3 and fused salt outlet of any following position, feeding device is provided with a spiral feeder in the interior of the upper part of the side of the molten salt reactor and the molten salt reactor separating screen, a feeding device. Preparing the biomass combustible gas of device can prevent the molten salt is solidified, in the reaction of a hot energy storage, the hot efficiency of the whole biomass gasification process.
NOVELTY - An alcohol-based fuel comprises 55-70 wt.% 93 gasoline, 10-15 wt.% methanol, 3-15 wt.% combustion improver, 0.1-0.5 wt.% additives, 0.003-0.1 wt.% speed retardant and 1-2 wt.% bio-oil.    USE - Alcohol-based fuel is used for car.    ADVANTAGE - The alcohol-based fuel is economical and environmentally-friendly. The car has reduced energy consumption and excellent performance characteristics, using the alcohol-based fuel.
NOVELTY - High energy liquid fuel comprises 4000 pts. wt. methanol and 3-6 pts. wt. acetone, 50-100 pts. wt. vegetable oil acid, 3-6 pts. wt. ferrocene, 100-200 pts. wt. fatty acid methyl ester, 2-5 pts. wt. pyridine, 20-50 pts. wt. xylene, 1-3 pts. wt. diethylhydroxylamine, 2-5 pts. wt. neopentyl glycol, 5-10 pts. wt. cetyl alcohol, 2-5 pts. wt. sodium petroleum sulfonate, 2-5 pts. wt. isooctanol, 1-3 pts. wt. flash point improving agent and 1-7 pts. wt. dimethyl carbonate as combustion-supporting additive.    USE - Useful as high energy liquid fuel.    ADVANTAGE - The liquid fuel ensures complete combustion, has high calorific value, and has good environment protection performance. The method is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the high energy liquid fuel, comprising (i) adding pyridine into methanol, performing modification reaction for 3 hours, adding cetyl alcohol, flash point improving agent and xylene and mixing for 1 hour to obtain mixture A; (ii) mixing vegetable oil acid, diethylhydroxylamine, dimethyl carbonate, acetone and isooctanol mixing for 2 hours to obtain mixture B; (iii) mixing fatty acid methyl ester, ferrocene, neopentyl glycol and sodium petroleum sulfonate, and allowing to stand for 2 hours to obtain mixture C; and (iv) mixing the mixture A, mixture B, and mixture C, and reacting by statically placing at room temperature and atmospheric pressure for 3-5 hours after complete fusion, where the preparation is performed at room temperature and atmospheric pressure.
NOVELTY - Environment-friendly methanol and gasoline containing composition comprises 20-30 pts. wt. of methanol, 10-30 pts. wt. of gasoline, 1-10 pts. wt. of polysorbate, 10-25 pts. wt. of tert-butanol, 10-20 pts. wt. of active agent and 5-15 pts. wt. of solubilizer.    USE - The environment-friendly methanol and gasoline containing composition is useful for gasoline engines and alternative fuel vehicles.    ADVANTAGE - The environment-friendly methanol and gasoline containing composition is inexpensive and non-hierarchical, exhibits good stability and increased corrosion resistance, and provides good combustion efficiency to the engines.
NOVELTY - A diesel oil composition comprises 22-37 wt.% methanol, 23-36 wt.% diesel oil, 0.3-9 wt.% diethylamino-tert-butanol, 0.8-2.6 wt.% butene, 0.1-1.3 wt.% hydrogen peroxide and 0.3-1.7 wt.% sodium bromide.    USE - Diesel oil composition is used for diesel engine.    ADVANTAGE - The diesel oil composition is environmentally-friendly and has excellent stability. The diesel engine obtained by the diesel oil composition has excellent damage resistance, corrosion resistance, and high combustion rate and suppressed generation amount of carbon monoxide and sulfur dioxide.
NOVELTY - Use of ferric hydroxide as in-situ biogas desulfurizing agent, is claimed.    USE - Ferric hydroxide is used as in-situ biogas desulfurizing agent (claimed).    ADVANTAGE - The desulfurizing agent avoids secondary pollution.
NOVELTY - Preparing biodiesel involves extracting Dunaliella salina using low polarity organic solvent to obtain biodiesel. The methanol and solid superacid catalyst are added to biodisel for ester exchange reaction. Methanol is removed by distillation under reduced pressure to obtain biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in easy, large scale and eco-friendly manner.
NOVELTY - Probiotic composition comprises bacteria chosen from Bacillus subtilis, B.stearothermophilus, Actinomycete ZI and B.amyloliquefaciens strain W1.    USE - The probiotic composition is useful for fermentation of straw (claimed).    ADVANTAGE - The probiotic composition significantly shortens fermentation or decay time period of the straw, as the composition contains significantly increased number of bacteria. The probiotic composition effectively ferments the straw in a environmentally-friendly manner.
NOVELTY - This new type utility claims of hydrogen and methane integrated analysis detect device in one marsh gas, comprising a gas chromatograph, a sample inlet of the gas chromatograph is provided with a flow path switching valve, the upper is provided with a flow path switching valve for feeding gas process amount of quantitative ring, a flow path switching valve is connected in parallel with an analysis flow path and shunt flow path, the flow path switching valve for switching the analysis flow path and shunt flow path, and the analysis flow path and flow outlet of flow path by the flow path switching valve connecting to the upper zirconium oxide detector. Rear using this utility new type can realize little hydrogen and constant for methane up in a single detector of analysis, and it does not need extra integral of signal amplification and stabilizing circuit and increases the reliability and accuracy.
NOVELTY - Bag cultivating Tremella comprises taking a corn core culture material having a component ratio of higher than 50%.    USE - The method is useful for bag cultivating Tremella (claimed).    ADVANTAGE - The method allows bag cultivation of the Tremella without environment protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing corn core culture material comprising selecting 55-58% of corn core, 22-25% of sawdust, 13% of rice bran, 5% of corn powder, 1% of sugar, 1% of gypsum and proper amount of water as raw materials, uniformly stirring the raw materials to prepare a material, adding proper amount of the water to the material, controlling the water content in the material to 60-65%, adjusting pH value of the mixed material to 7.5-8, and fermenting the mixed material for 5-8 days.
NOVELTY - Ultra-micro powder of prepared rhizome of Rehmannia extract, is claimed. The ultra-micro powder of prepared rhizome of Rehmannia extract has granularity of 1-10 microns, bacterial count of no more than 10000 colony forming units (cfu)/g, and mold or yeast count of 100 cfu/g.    USE - The ultra-micro powder of prepared rhizome of Rehmannia extract is useful for treating palpitation, irregular menstruation, uterine bleeding, liver-kidney-yin deficiency, hot flashes, night sweat, spermatorrhea, dizziness, anxiety, tumor and tinnitus, and improving memory, enhancing immunity, delaying aging, providing antioxidant effect (all claimed).    ADVANTAGE - The method is suitable for industrialization, and does not use chemicals and cause radiation pollution, and prepares the extract at a yield of 25% or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned ultra-micro powder of prepared rhizome of Rehmannia extract, which involves (a) drying the rhizome of Rehmannia, and cooling the dried rhizome, (b) crushing the rhizome, and sieving the crushed rhizome to obtain powder, (c) adding water to the obtained powder and homogenizing, and (d) adding the obtained product to high-pressure homogenizer.
NOVELTY - A biodiesel oil is prepared by reacting soybean oil, methanol and catalyst at 55-65 degrees C for 15-30 minutes at rate of 200-300 revolutions/minute, cooling, washing, rotary evaporating, standing in separating funnel for 30 minutes, and gas chromatography separating.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method has mild reaction condition, short reaction time, and high conversion rate.
NOVELTY - A biodiesel oil is prepared by pretreating oil, heating, cooling, filtering, esterification reacting in methanol and sulfuric acid at 60-70 degrees C for 0.5 hour, heating, cooling, standing in separating funnel, discharging lower liquid layer, adding acid catalyst, washing with distilled water, heating, and distilling.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method utilizes waste, saves energy and reduces pollution.
NOVELTY - A biodiesel oil is prepared by reacting 30 g refined tea seed oil and potassium hydroxide-methanol solution at 55-60 degrees C for 60-80 minutes, stirring, standing, water washing upper layer solution, drying with anhydrous magnesium sulfate, and performing saponification.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method utilizes waste, increases farmer income and improves economic benefit.
NOVELTY - The generator has a main portion (1) which is provided with gourd spherical container (2). A storage bottle (3) is arranged in kipp generator main portion and is connected with the gourd spherical container through the piston (4).    USE - Kipp generator for preparing hydrogen gas.    ADVANTAGE - The controllable operation and uniform speed of generator can be achieved and the raw material can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view,atoc view of kipp generator.    Kipp generator main portion (1)    Gourd spherical container (2)    Storage bottle (3)    Piston (4)
NOVELTY - A biodiesel is prepared by mixing Chlorella powder and distilled water, reacting with methanol at 250-270 degrees C for 10-30 minutes at pressure of 5-10 MPa, raising temperature, cooling to room temperature, transferring into Buchner funnel, filtering under reduced pressure, adding distilled water, eluting in methanol, extracting in n-hexane, separating, and drying.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The biodiesel reduces energy consumption.
NOVELTY - A biodiesel oil is decolored by performing transesterification biodiesel oil, adding 5-25 wt.% hydrogen peroxide, heating at 70-90 degrees C, stirring, reacting for 18-25 minutes, centrifuging, removing upper phase, spectrum scanning, decoloring, and removing impurity.    USE - Method for decoloring biodiesel oil (claimed).    ADVANTAGE - The simple method has fast decoloring speed and high recovery efficiency.
NOVELTY - A biodiesel oil is prepared by hydrolysis reacting 100 pts. wt. waste oil and 40-60 pts. wt. acid catalyst, heating to boil, stirring for 2-6 hours, separating to obtain upper layer fatty acid and lower layer gum and water, performing esterification reaction of fatty acid in methanol and acid catalyst at 60-80 degrees C for 2-6 hours, separating, washing, drying, and distilling.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method utilizes waste, reduces environment pollution and relieves energy resource.
NOVELTY - A biodiesel oil is synthesized by pretreating crude castor oil, heating, cooling, filtering, esterification reacting with methanol and sulfuric acid at 60-70 degrees C for 0.5 hour, heating, cooling, standing to obtain liquid and crude biodiesel oil, mixing acid catalyst and crude biodiesel oil, washing with distilled water, heating, and distilling under reduced pressure.    USE - Method for synthesizing biodiesel oil (claimed).    ADVANTAGE - The method utilizes waste, saves energy consumption and reduces pollution.
NOVELTY - Digesting organic material into biogas comprises: pretreating the organic material by thermal, mechanical and/or chemical treatments; treating the pretreated organic material with at least two carbohydrases to obtain a weight ratio of soluble oligosugars to monosugars of 1000:1-1:1, or with a composition comprising at least an endo-carbohydrase and an exo-carbohydrases, where the weight ratio of endo-carbohydrase and exo-carbohydrase is 2:1-100:1; separating the liquid fraction from the solid fraction of the enzyme-treated organic material; and digesting the liquid fraction to form biogas.    USE - The process is useful for digestion of organic material into biogas (claimed), preferably methane.    ADVANTAGE - The process: lowers overall retention times without the loss of gas yield compared to conventional processes; is capable to treat all kind of digestible organic material such as sludge or other organic material, e.g. bacterial sludge or other bacterial organic waste; is energy efficient; requires less enzyme, thus producing biogas in a more stable and economical manner with high yield and rate; and provides more consistent bacterial population in the methane producing reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an enzyme composition comprising at least an endo-carbohydrase and an exo-carbohydrase, where the weight ratio of endo-carbohydrase and exo-carbohydrase is 2:1-100:1.
NOVELTY - The humidification device has a fuel process system water trap (40) that supplies water to a humidifier (20) and is connected to the air electrode exit of a fuel cell stack (10). The humidifier is connected to the fuel anode exit of a stack. A pumping unit (60) re-circulates the water stored the water within an air process system (APS) water trap (50). The APS water trap keeps the water outlet (22) installed at the bottom of the humidifier. The humidifier is ejected from the air electrode and is connected in store after a recycle line (52) within the humidifier.    USE - Humidification device for a fuel cell.    ADVANTAGE - The fuel process system water trap supplies water to a humidifier and is connected to the air electrode exit of a fuel cell stack and the pumping unit re-circulates the water stored the water within air process system water trap, thus improves the by-pass factor of the dry air supplied to the fuel cell stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a humidification method for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a humidification device. (Drawing includes non-English language text).    Fuel cell stack (10)    Humidifier (20)    Water outlet (22)    Fuel process system water trap (40)    Air process system water trap (50)    Recycle line (52)    Pumping unit (60)
NOVELTY - Treatment of waste liquid involves acidifying, oxidizing, biochemically-treating, neutralizing, flocculating, settling and separating and obtaining mother liquid.    USE - Treatment of waste liquid used for producing liquid fertilizer for agriculture and forestry.    ADVANTAGE - The method efficiently and economically treats waste liquid. The fertilizer obtained using the liquid improves the yield of crops by 20-40%.
NOVELTY - 5-((2R)-2-(Benzylamino)propyl)-1-(3-(benzoyloxy)propyl)-7-cyano-indoline compound (IV) is catalytically hydrogenated, to obtain (1(3-benzoyloxy-propyl)-5-(2-aminopropyl)7-cyano)indoline compound (V). The obtained compound is reacted under basic condition, to obtain 2-(2,2,2-trifluoroethoxy)phenoxy ethyl methanesulfonate compound (VI) which is then condensed, to obtain 1-(3-(4-fluoro-benzoyl)propyl)-5-((2R)-2-(2-(2-(2,2,2-difluoro-ethoxy)phenoxy)ethylamino)propyl)indolyl-7-cyano compound (VII). The product is hydrolyzed under alkaline condition, to obtain silodosin.    USE - Preparation of silodosin (claimed).    ADVANTAGE - The method efficiently and economically provides high-purity silodosin having yield of 20-43% without causing pollution to environment in short period of time.    DETAILED DESCRIPTION - 7-Cyano-indoline as starting material is reacted with indoline containing benzoyloxy propyl group, to obtain 1-(benzoyloxy-propyl)-7-cyano-indoline compound (I). Then, the obtained compound is reacted with 2R-2-((phenylmethyl) amino)-propionic acid chloride compound (II) and subjected to Friedel-Crafts acylation reaction, to obtain chiral intermediate 5-((2R)-2-(benzylamino)-1-propyl)-1-(3-(benzoyloxy)propyl)-7-cyano-indoline compound (III). The obtained compound is reduced using triethylsilane, to obtain 5-((2R)-2-(benzylamino)propyl)-1-(3-(benzoyloxy)propyl)-7-cyano-indoline compound (IV) which is then catalytically hydrogenated, to obtain (1(3-benzoyloxy-propyl)-5-(2-aminopropyl)7-cyano)indoline compound (V). The obtained compound is reacted under basic condition, to obtain 2-(2,2,2-trifluoroethoxy)phenoxy ethyl methanesulfonate compound (VI) which is then condensed, to obtain 1-(3-(4-fluoro-benzoyl)propyl)-5-((2R)-2-(2-(2-(2,2,2-difluoro-ethoxy)phenoxy)ethylamino)propyl)indolyl-7-cyano compound (VII). The product is hydrolyzed under alkaline condition in presence of hydrogen peroxide, to obtain silodosin.
NOVELTY - Preparation of wood fiber biomass gas gel involves pulverizing wood fiber biomass to size of 160 meshes, dissolving pulverized material in solution containing 2-10 %mass lithium chloride and dimethyl sulfoxide, pouring solution into a mold at -196 to -20 degrees C, freeze-thawing for 1-24 hours, repeating processing for 2-10 times, placing solution in immersion bath containing solvent, forming a gel, and performing supercritical drying.    USE - Preparation of wood fiber biomass gas gel (claimed).    ADVANTAGE - The wood fiber biomass gas gel is produced efficiently by simple method.
NOVELTY - The method involves defining range of pressure loss of supply gas in a cell. Pressure loss of the supply gas and deflection amount of the gas along gas flow paths of gas diffusion layers (24a, 24b) is calculated. Range of deflection amount of gas is defined based on the defined pressure loss. A fuel cell is assembled such that deflection amount of the gas along flow path of the gas diffusion layers is set to the defined deflection amount range. Tension elastic modulus of the gas diffusion layer and contact pressure of the gas diffusion layer are calculated.    USE - Method for manufacturing a fuel cell.    ADVANTAGE - The fuel cell is assembled such that the deflection amount of the gas along flow paths of the gas diffusion layers is set to the defined deflection amount range, so that pressure loss of the supply gas in the cell can be adjusted, size of a fuel cell system can be simplified, cost of the system can be reduced and usability of the system can be improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a fuel cell    (2) a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a fuel cell.    Anode (22a)    Cathode (22b)    Gas diffusion layers (24a,24b)    Separator (26a,26b)    Fuel gas flow channel (27)
NOVELTY - The manufacturing method involves preparing an electrode ink containing a metal precursor elemental-metalized by reduction. An electrode (2) is formed by coating the electrode ink to an electrolyte layer (4). A fuel cell (S) is obtained. The fuel cells are stacked in multiple numbers to obtain a cell laminated body (15). A liquid fuel which reduces the metal precursor is supplied with respect to the cell laminated body.    USE - Manufacturing method for a fuel cell.    ADVANTAGE - The liquid fuel which reduces the metal precursor is supplied with respect to the cell laminated body which ensures that the need of the reduction firing process is eliminated and the fuel cell is manufactured by a simple and low-cost process. The electric power generation performance of the fuel cell is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Electrode (2)    Electrolyte layer (4)    External circuit (13)    Cell laminated body (15)    Fuel cell (S)
NOVELTY - A catalyst ink comprises a dispersion medium containing water and an organic solvent, a catalyst carrier having electroconductivity which supports the catalyst, and an ionomer having proton-conductivity dispersed in mixture, where an adsorption amount (BI value) of the ionomer per surface area to a catalyst is calculated using ionomer adsorption amount (IOv) and surface area (CAs) and is computed by the expression as per given in the specification through a quartz crystal oscillation microbalance measuring method.    USE - Catalyst ink for forming electrode that is utilized for manufacturing fuel cell.    ADVANTAGE - The catalyst ink increases gas contact opportunity to the catalyst in a three-phase interface.    DETAILED DESCRIPTION - A catalyst ink comprises a dispersion medium containing water and an organic solvent, a catalyst carrier having electroconductivity which supports the catalyst, and an ionomer having proton-conductivity dispersed in mixture, where an adsorption amount (BI value) of the ionomer per surface area to a catalyst is calculated using ionomer adsorption amount (IOv) and surface area (CAs) and is computed by the expression as per given in the specification through a quartz crystal oscillation microbalance measuring method, the surface area (CAs) of the catalyst in the pore distribution from which a pore size of greater than or equal to 10 nm is distributed over the circumference of a catalyst and the BI value is 0.4-3.0. An INDEPENDENT CLAIM is also included for a method for manufacturing catalyst ink.
NOVELTY - Alcohol based civilian fuel comprises main fuel, secondary fuel, co-solvent and oxidizing agent, and is prepared by mixing (wt.%): methanol as main fuel (70-75), hydrocarbon fuel as secondary fuel (8-15), acetone (5-10) and petroleum ether (0.5-1) as co-solvent, and sodium salicylate (1.5-4), polyoxyethylene ester (0.5-1) and hydrogen peroxide (3-8) as oxidizing agent.    USE - Alcohol based civilian fuel.    ADVANTAGE - The alcohol based civilian fuel is safe, economic and eco-friendly, and has high calorific value.
NOVELTY - Acetylene bridged linkers are new.    USE - As linker for the production of metal organic frameworks which is used for adsorbing, storing and/or releasing gas (preferably methane-containing mixture or methane, and hydrogen) (claimed).    ADVANTAGE - The compounds (I) provide metal-organic frameworks with an enhanced ability to adsorb and desorb high amounts of gases, in particular methane or hydrogen. The metal-organic frameworks obtained by the compound (I) have high porosity and exhibit surprisingly high surfaces. The surfaces of the metal-organic frameworks are greater than or equal to 1000 m2/g (BET) or greater than or equal to 2000 m2/g (BET), greater than or equal to 2500 m2/g (BET) or greater than or equal to 3000 m2/g (BET).    DETAILED DESCRIPTION - Acetylene bridged linkers of formula (I) are new.    R1 and R2=H, Bn or CH3;    R=selected from carbons and/or hydrocarbons; has a Cn symmetry with n greater than or equal to 2; and comprises at least one acetylene group.    INDEPENDENT CLAIMS are included for the following:    (1) new intermediate selected from 2-benzyloxy-4-trimethylsilanylethynyl-benzoic acid methyl ester, and 2-benzyloxy-4-ethynyl-benzoic acid methyl ester; and    (2) metal organic frameworks comprising at least one compound (I) with R1=R2=H as linker.
NOVELTY - Kitchen waste fertilizer is prepared by collecting kitchen waste after good meal, adding the waste in container, smashing the waste, injecting suitable quantity of water, adding leavening agent to the smashed mixture, stirring the mixture, sealing the stirred mixture, fermenting the sealed mixture for 20-30 days, obtaining fermented kitchen waste black liquid, adding powdered activated carbon or hydrogen peroxide to observe odor, and diluting the fermented broth using water.    USE - As kitchen waste fertilizer.    ADVANTAGE - The fertilizer is prepared simply and cost-effectively, prepared in home and convenient to use, and does not cause any harm to soil and flowers.
NOVELTY - Wettable powder fertilizer is prepared using 5000-800 billion spores Bacillus licheniformis, 2000-400 billion spores Bacillus subtilis spores, 210-290 g silica, 80-l20 g calcium carbonate, 25-35 g anticaking agent, 230-310 g kaolin, 40-60 g boron, 25-35 g ferrous sulfate, 100-l40 g zinc sulfate, 25-35 g manganese sulfate, 8-12 g sodium silicate and remainder carrier.    USE - As wettable powder fertilizer.    ADVANTAGE - The wettable powder is convenient to use and has high fertilizing efficiency by acting directly in rhizosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the wettable powder, which involves adding calcium carbonate, anticaking agent, kaolin, boron, ferrous sulfate, zinc sulfate, manganese sulfate and sodium silicate into mixer for mixing and drying the mixed material and adding the dried material into blender and then adding B.licheniformis spores, B.subtilis spores and anticaking agent and stirring uniformly and crushing the product using 400 mesh sieve airflow pulverizer.
NOVELTY - Preparation of oxyfluorfen water suspension comprises adding oxyfluorfen, wetting agent, dispersant, suspension stabilizer, antifreeze agent, thixotropic agent, and water into autoclave, and stirring to obtain slurry; coarse grinding, and fine grinding; adding to reaction kettle, adding defoamer and water, stirring, sampling to carry out analysis to obtain qualified products, adding to storage tank, and packaging.    USE - Method for preparation of oxyfluorfen water suspension (claimed).    ADVANTAGE - The method is simple and energy-saving, uses water to replace organic solvent which solves environmental pollution and security risks problems, and reduces cost.    DETAILED DESCRIPTION - Preparation of oxyfluorfen water suspension comprises adding oxyfluorfen, wetting agent, dispersant, suspension stabilizer, antifreeze agent, thixotropic agent, and water at mass ratio of 24.2-24.4 wt.%, 3-5 wt.%, 2-3 wt.%, 4-5 wt.%, 1-2 wt.%, 0.2-0.5 wt.%, and 60-55 wt.% into autoclave, and stirring for 1 hour to obtain slurry; adding to colloid mill to carry out coarse grinding for 2 hours, and fine grinding for 2.5-3.5 hours in sand mill to obtain less than 3 mu m particles; adding to reaction kettle, adding 0.02-0.05 wt.% defoamer and 100 wt.% water, stirring for 1 hour, sampling to carry out analysis to obtain 240 g/L qualified products, adding to storage tank, and packaging. The unqualified products are added with water until it passes qualification.
NOVELTY - Extraction of potassium-magnesium fertilizer, boric acid and lithium carbonate from sodium sulfate salt lake comprises evaporating, acidifying mother liquor, solvent extracting, freezing and extracting to obtain boric acid; evaporating raffinate to remove sodium salt and freezing to obtain potassium-magnesium fertilizer; purifying mother liquor using zeolite and desorption agents, freezing and evaporating to obtain potassium nitrate; concentrating mother liquor, adding sodium carbonate, washing and drying to obtain lithium carbonate.    USE - Method for extracting potassium-magnesium fertilizer, boric acid and lithium carbonate from sodium sulfate salt lake (claimed).    ADVANTAGE - The simple and eco-friendly method has high product quality, high resource utilization and no wastewater discharge.
NOVELTY - Preparing organic fertilizer, involves weighing livestock and poultry manure, leaves, crop straw, green manure and slurry, adding water to weighed materials, stirring and mixing uniformly to obtain mixture, introducing microbial inoculum to the mixture, performing fermentation, recovering compound fertilizer, drying the compound fertilizer, crushing dried compound fertilizer in a crusher, sieving crushed compound fertilizer, adding sieved powder to granulator, and granulating to obtain granule.    USE - The method is useful for preparing organic fertilizer (claimed) which is useful for protecting crops, and improving disease resistance.    ADVANTAGE - The method reduces pollution, and prepares fertilizer that is rich in organic material, amino acid, vitamin, plant hormone and other active substances.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves weighing 35-55 pts. wt. livestock and poultry manure, 5-10 pts. wt. leaves, 13-18 pts. wt. crop straw, 20-25 pts. wt. green manure and 30-40 pts. wt. slurry, adding water to weighed materials, stirring and mixing uniformly to obtain mixture, covering fermented material using thin film, introducing microbial inoculum to the mixture, performing fermentation at 25-30 degrees C for not less than 7 days, recovering compound fertilizer, drying the compound fertilizer, crushing dried compound fertilizer in a crusher, sieving crushed compound fertilizer through 60-100 meshes sieve, adding sieved powder to granulator, and granulating to obtain granule.
NOVELTY - Mushroom culture medium comprises 10-45 pts. wt. kelp residue, 10-25 pts. wt. wheat bran, 1-3 pts. wt. gypsum, and 1-3 pts. wt. cane sugar.    USE - As mushroom culture medium.    ADVANTAGE - The culture medium is prepared cost-effectively.
NOVELTY - Cultivating material comprises 10-25 pts. wt. Poaceae leaves/grass, 5-15 pts. wt. cotton seed hull, 5-15 pts. wt. wheat, 40-80 pts. wt. mulberry tree/branch, and 100-130 pts. wt. water.    USE - The material is useful for cultivating mushroom (claimed).    ADVANTAGE - The cultivating material is prepared cost-effectively and stably, suitable for large scale production, and reduces the production cost-effective of mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the cultivating material, which involves crushing and mixing the above-mentioned raw materials uniformly, placing in a crusher to crush, sieving through 10-40 meshes sieve, placing the crushed raw material into water, mixing uniformly, paving on the ground to 0.3-0.6 m thin layer, providing a hole on the base pair sequence with the diameter of 8-10 cm and space between the centers of adjacent holes is 12-15 cm, fermenting at normal temperature for 4 days, performing enzymolysis on the fermented product, placing into a plastic bag, where each bag contains 2-3 kg, heating for 5-7 hours by steaming, cooling the substrate to 30 degrees C, inoculating fungi into the bag, culturing, sealing, placing in summer for 15-20 days and winter for 20-30 days, spraying water for irrigation for 4-7 days and opening the bag after 5-7 days to obtain product.
NOVELTY - Cultivating material comprises 10-25 pts. wt. Poaceae leaves/grass, 5-15 pts. wt. cotton seed hull, 5-15 pts. wt. wheat, 45-75 pts. wt. saw dust, and 100-130 pts. wt. water.    USE - The material is useful for cultivating mushroom (claimed).    ADVANTAGE - The cultivating material is prepared cost-effectively and stably, suitable for large scale production, and reduces the production cost-effective of mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the cultivating material, which involves crushing and mixing the above-mentioned raw materials uniformly, placing in a crusher to crush, sieving through 10-40 meshes sieve, placing the crushed raw material into water, mixing uniformly, paving on the ground to 0.2-0.5 m thin layer, providing a hole on the base pair sequence with the diameter of 8-10 cm and space between the centers of adjacent holes is 12-15 cm, fermenting at normal temperature for 4 days, performing enzymolysis on the fermented product, placing into a plastic bag, where each bag contains 2-3 kg, heating for 5-7 hours by steaming, cooling the substrate to 30 degrees C, and inoculating fungi into the bag to obtain product.
NOVELTY - Flower fertilizer comprises 10-15 pts. urea, 12-18 pts. potassium mineral powder, 5-10 pts. strain powder, 20-30 pts. sheep manure, 15-20 pts. soybean hull, 18-22 pts. peat, and 13-15 pts. additive.    USE - Used as a flower fertilizer.    ADVANTAGE - The fertilizer is natural, improves the soil quality to prevent deterioration, soil surface crust and soil compaction phenomenon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the flower fertilizer, comprising mixing peat, soybean hull and sheep manure evenly in sealed fermentation tank, and fermenting for 15-25 hours; mixing urea, potassium mineral powder, strain powder, rice bran and water, adding the fermented product, mixing, and granulating in a granulator.
NOVELTY - Fertilizer comprises 5-10 pts. wt. cation exchange resin, 10-20 pts. wt. sea-buckthorn, 10-20 pts. wt. trumpet creeper, 40-50 pts. wt. chicken manure, 30-50 pts. wt. powdered rock phosphate, 1-2 pts. wt. photosynthetic bacteria, 2-4 pts. wt. ammonium sulfate, and 1-2 pts. wt. ferment bacteria.    USE - The fertilizer is useful for enhancing soil water retention (claimed).    ADVANTAGE - The fertilizer: is simple and easy to use; reduces the salt content of the soil; enhances the activity of microorganism and enzymes in the soil; promotes plant root system to grow; and improved saline-alkali land.
NOVELTY - Preparation of cyclopentyl-triazolo-pyrimidine intermediate involves preparing 2-(((2S,3R,4R)-4-amino-2,3-dimethoxycyclopentyl)oxy)ethan-1-ol (I) by reacting dimethoxycyclopentane compound (II) and 2-hydroxy-1,3-dioxathiolan-2-one (III) or 1,3-dioxathiolan-2-one (IV) as raw materials under alkaline conditions, removing O-sulfate or O-sulfite, and eliminating amino-protecting group.    USE - Preparation of cyclopentyl-triazolo-pyrimidine intermediate (claimed).    ADVANTAGE - The method enables the preparation of cyclopentyl-triazolo-pyrimidine intermediate with high yield, by environmentally-friendly and economical process.    DETAILED DESCRIPTION - Preparation of cyclopentyl-triazolo-pyrimidine intermediates involves preparing 2-(((2S,3R,4R)-4-amino-2,3-dimethoxycyclopentyl)oxy)ethan-1-ol of formula (I) by reacting dimethoxycyclopentane compound of formula (II) and 2-hydroxy-1,3-dioxathiolan-2-one of formula (III) or 1,3-dioxathiolan-2-one of formula (IV) as raw materials under alkaline conditions, removing O-sulfate or O-sulfite, and eliminating amino-protecting group.    R1R2=benzyloxycarbonyl, phthaloyl, benzyl, or amino-protecting group.
NOVELTY - Composite microbial inoculum comprises 1x 1010-1x 1012 colony forming units (cfu)/ml Pseudomonas strain B6-15 and 1x 1010-1x 1012 cfu/ml Pseudomonas strain B5-16, where the total bacterial number is 2x 1010-2x 1012 cfu/ml.    USE - The microbial inoculum is useful in low-temperature compost (claimed).    ADVANTAGE - The microbial inoculum shortens the time required during the heating stage of compost; and improves the compost temperature, and thus it facilitates easy heating process of the compost in domestic northern areas at winter low temperature environmental conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing microbial inoculum, comprising (i) inoculating original strain of Pseudomonas strain B6-15 and Pseudomonas strain B5-16 into a solid culture medium under aseptic condition, culturing for 1-2 days at 15-25 degrees C, and activating the strain; (ii) inoculating the activated strain of the step (i) into a neutral red (NR) liquid culture medium under aseptic condition, and shaking while culturing at 15-25 degrees C for 1-2 days to obtain a primary seed solution; and (iii) culturing the primary seed solution containing Pseudomonas strain B6-15 and Pseudomonas strain B5-16 in a fermentation tank at 20 degrees C under the condition of mixing culture for 3-5 days to obtain the product.
NOVELTY - Preparation of methionine comprises taking 15-16 wt.% casein, 2 wt.% hydrolase, 80-81 wt.% water, 2 wt.% sodium hydroxide, aqueous sodium hydroxide and hydrochloric acid, filling reactor with water, stirring, adding sodium hydroxide, heating at 50-55 degrees C, adding casein and hydrolase, carrying out hydrolysis, stirring for 4-5 hours, crystallizing using sodium hydroxide and hydrochloric acid to adjust pH value to 5.74, standing for 10 hours, centrifuging, discarding water, vacuum drying at 65-75 degrees C for 9-11 hours, crushing and sieving.    USE - Method for preparing methionine (claimed) used for treating cirrhosis, myocardial disease and depression, lowering blood pressure, detoxifying, enhancing body metabolism, dysplasia in livestock, promoting weight loss, treating kidney deficiency and muscle atrophy.    ADVANTAGE - The method is simple, environment-friendly and easy to operate.
NOVELTY - Producing valine comprises adding water into a reaction kettle, stirring, adding sodium hydroxide, heating and adding N-acetyl-DL-valine and acylase and reacting by stirring, transferring the reaction material into a crystallization kettle, adding aqueous sodium hydroxide and hydrochloric acid and allowing to stand for 10 hours for complete crystallization of valine, discharging the liquid, carrying out centrifugal separation to remove small amount of water from valine crystals, subjecting the crystals for vacuum drying in a dryer, crushing, sieving and packing the valine product.    USE - The method is useful for producing valine (claimed).    ADVANTAGE - The method is simple without any waste discharge and high temperature-high pressure reaction, and produce good quality product in batch production. The valine is an essential amino acid for human body e.g. adult men requirement of 10 mg/kg of body weight/day, suitable for treating liver failure and accelerating wound healing (as therapeutic agent and nutritional supplement).    DETAILED DESCRIPTION - Producing valine comprises: (i) adding 74% water into a reaction kettle, stirring, adding 1% sodium hydroxide, heating at 55-60 degrees C and adding 19-20% N-acetyl-DL-valine and 5-6% acylase and reacting for 4-5 hours by stirring; (ii) transferring the reaction material into a crystallization kettle, adding aqueous sodium hydroxide and hydrochloric acid under room temperature and adjusting pH to 5.96, and allowing to stand for 10 hours for complete crystallization of valine; and (iii) discharging the liquid, carrying out centrifugal separation to remove small amount of water from valine crystals, subjecting the crystals for vacuum drying in a dryer at 65-75 degrees C for 8-10 hours, crushing, sieving and packing the valine product.
NOVELTY - Base fertilizer comprises 40-42 wt.% of pig manure, 8-10 wt.% of Photinia leaves, 6 wt.% of licorice, 8 wt.% of corn straw, 6 wt.% of cottonseed, 6 wt.% of beer lees, 8 wt.% of canal mud, 1 wt.% of fermenting agent, 1 wt.% of synergistic agent, 10 wt.% of ammonium hydrogen carbonate, 2 wt.% of calcium magnesium phosphate, 1 wt.% of potassium chloride, 0.2 wt.% of zinc sulfate, 0.5 wt.% of borax and 0.3 wt.% of copper sulfate.    USE - The base fertilizer is useful for cultivating Photinia serrulata (claimed).    ADVANTAGE - The base fertilizer promotes the activation of roots in soil, inhibits the growth of soil pathogens, and removes toxins in the soil.    DETAILED DESCRIPTION - Base fertilizer comprises 40-42 wt.% of pig manure, 8-10 wt.% of Photinia leaves, 6 wt.% of licorice, 8 wt.% of corn straw, 6 wt.% of cottonseed, 6 wt.% of beer lees, 8 wt.% of canal mud, 1 wt.% of fermenting agent, 1 wt.% of synergistic agent, 10 wt.% of ammonium hydrogen carbonate, 2 wt.% of calcium magnesium phosphate, 1 wt.% of potassium chloride, 0.2 wt.% of zinc sulfate, 0.5 wt.% of borax and 0.3 wt.% of copper sulfate. The base fertilizer is prepared by crushing the pig manure, Photinia leaves, licorice, corn straw, cottonseed, beer lees and canal mud, crushing the fermenting agent, then mixing with crushed raw material, transferring into a fermentation tank, adding water into the tank, mixing, sealing the tank using plastic film, fermenting at autumn season for 28-32 days to obtain organic fertilizer mixture, crushing the synergistic agent, ammonium hydrogen carbonate, calcium magnesium phosphate, potassium chloride, zinc sulfate, borax and copper sulfate, mixing the crushed powder with organic fertilizer mixture, and fermenting.
NOVELTY - A golf lawn fertilizer comprises 20-50 pts. wt. phellodendron, 10-30 pts. wt. oil-tea camellia seed bran, 10-15 pts. wt. garden waste, 5-10 pts. wt. sodium alginate, 0.1-3 pts. wt. fish meal, and 0.01-0.09 pts. wt. effective microorganism (EM) agents.    USE - A golf lawn fertilizer.    ADVANTAGE - The fertilizer has comprehensive nutrition, fine granularity, and is durable, affordable, salt tolerant and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of golf lawn fertilizer comprising:    (A) respectively taking each raw material;    (B) crushing garden waste into particles with particle diameter of 2-4 mm;    (C) uniformly mixing spare oil tea platinum, rapeseed bran, garden waste particles, seaweed residue, and fish meal, and adjusting the water content at 50-70% to obtain the mixed material;    (D) fermenting for 5-24 days;    (E) drying the fermented material, and reducing the water content to less than 30%;    (F) drying the material, taking and sieving through a sieve of 30-50 meshes to form composite material;    (G) granulating, and controlling the grain diameter at 0.55-3.35 mm;    (H) sieving the spared granulating material, grading, taking the unqualified grain and returning to step (F) to be qualified grain for sieving;    (I) drying the spared and screened material until the moisture content is less than 3.5% to obtain a secondary dried material; and    (J) classifying the secondary dried material and taking the grain diameter at 0.55-1.30 mm, and classifying turf area and serving table for special fertilizer with a grain diameter at 1.31-3.35 mm, classifying track area for special fertilizer, and respectively packing.
NOVELTY - The method involves collecting waste and organic component. The organic component is presented in a baking box at 105 degree centigrade. Mass ratio of calcium oxide is about 95:5, 90:10 and 85:15. Extrusion molding diameter and length are about 15 mm and 150 mm, respectively. RDF fuel is filled in a fixed bed gasification device comprising a raw material storage chamber, an electric heating furnace and a bath gas purifying device. Hydrogen-rich synthesis gas is obtained. The furnace is connected with a temperature control device and a water steam generator.    USE - Hydrogen-rich synthesis gas preparing method.    ADVANTAGE - The method enables reducing raw material utilization rate and urban household rubbish processing difficulties in a simple manner and ensuring environment friendly.
NOVELTY - Butanol is produced by supplying temporary electron which can take both oxidant and reductant forms to butanol production microorganisms (2) which produce metabolite (7) which contains butanol on a proliferation cooperating target while consuming a substrate (3) via an electronic media substance (5).    USE - A butanol production method for biofuel, raw material for chemical compounds such as isoprene, isobutene, and butene, and combustion improver of biofuel.    ADVANTAGE - Yield and production efficiency are improved, and cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the butanol production method.    Butanol production microorganisms (2)    Substrate (3)    Culture solution (4)    Electronic media substance (5)    Metabolite (7)    Electrode (9)
NOVELTY - Particles comprise a magnetic material containing a silica-based layer, comprising magnetic microparticles with a silica-based surface, and a layered double hydroxide deposited on the surface of the microparticles.    USE - Particles are used for recovering anion e.g. phosphate anion from aqueous solution and catalyzing chemical reaction by heterogeneous catalysis e.g. vegetable oil transesterification reactions for production of biodiesel, reaction of soybean oil with methanol, carrier for biochemical molecule e.g. enzyme, ribonucleic acid, deoxyribonucleic acid and iron porphyrins immobilized on layered double hydroxide, removing heavy metal contamination from water, and biosensing application.    ADVANTAGE - The particles have excellent stability during repeated phosphate adsorption/desorption cycles, selectivity with respect to phosphate ions, large specific surface area, and are economically and rapidly manufactured by simple process. The magnetic particles have reduced energy loss with respect to magnetic hysterisis. Since the particles have high anion adsorption capacity, magnetic separability and simple regeneration, anion is recovered from wastewater by economical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of magnetic particles, which involves mixing magnetic microparticles with silica-based surface in an aqueous solution at pH of 7 with a dispersion of layered double hydroxide at pH of 7, and ultrasonicating the obtained mixture for depositing the layered double hydroxide on the surface of the microparticles;    (2) usage of particles for recovering anion, preferably phosphate anion from aqueous solution;    (3) usage of particles for catalyzing chemical reaction by heterogeneous catalysis; and    (4) usage of particles as a carrier for a biochemical molecule, preferably an enzyme, immobilized on layered double hydroxide.
NOVELTY - This utility model claims one kind of cultivating edible fungi by using kitchen garbage's system, belonging to the edible fungi cultivation system. The kitchen waste processing system is composed of a bag making subsystem and the edible mushroom fungus inoculating sub-system are connected in turn; The system by inoculating edible fungi subsystem set kitchen waste processing machine sub-system, the kitchen garbage disposal machine as edible mushroom fungus culture system for cultivation raw material's, so as to realize the culture's edible fungi. The system is simple in structure, convenient to operate, and it can realize by using kitchen garbage for producing edible fungi industrial cultivation. The pleurotus nebrodensis mushroom cultivation and production of edible fungi's oyster mushroom, pleurotus eryngii, mushroom, hericium erinaceus, needle mushroom, mushroom and so on.
NOVELTY - The utility model claims one container type methane purifying membrane method purification system, comprising a movable container's desulfurizing, dehydrating and unit are connected in turn, a compressor, a purifying unit, a heat exchanger and a film of gas purifying unit, said unit is connected with the desulfurizing, dehydrating and anaerobic fermentation tank biogas generated gas source. The utility model purifying device is integrated in the container, the technique flow is short, saves floor area, can be miniaturized, mobile; biogas purifying is made of polymer film for separating carbon dioxide and methane, less investment, low energy consumption, marsh gas before entering the film purifying the purifying and removing impurity, ensures purifying quality's gas.
NOVELTY - The utility model claims one non-distillation water purifier's bio-purifying device for front, belonging to the field of household pure water preparing technology field, aiming at overcoming the comparison's common non-distillation household water purifier's's the removing rate of heavy metal ion in water and some organic pollution impurity not's. The utility model comprises a tap water, distillation water purifier and water inlet valve's up said non-distillation water purifier, comprising a purifying tank is equipped with filter layer in said biological purification groove, is provided with a clean water tank and said filter layer's lower part is provided with a pressurizing pump is connected with the said water inlet valve is set between the said water purifying tank by the pipeline. This utility model is suitable for installing non-distillation water purifier for household tap water prior to the treatment.
NOVELTY - This utility model claims one kind of active sludge microorganism selection device, the device is composed of multiple multi-tube mixer in turn connected point's type distributor and biological selector, wherein said mixer is provided with a sewage inlet and a sludge inlet corresponding to the sewage inlet is equipped with a sewage device, said biological selector is equipped with baffle plate. Characteristic strong absorption capability's utility model's active sludge microorganism selection device makes full use of the microorganism's stronger microscopic examination active to the organic substance in the sewage has's before to the sewage treatment, the sewage and active sludge to fully's, the active sludge and sludge to separate, from the source up to remove inactive and active difference cannot be the whole reaction function's sludge, so as to ensure the active sludge is biochemical treatment process, the microorganism fully exert its catabolic metabolism function, improves the treatment effect's.
NOVELTY - This utility model claims one kind of solar energy as heating heat source's constant-temperature biogas fermentation tank, mainly comprising a solar water heater, a hot water buffer, a spiral heat exchanger, an automatic temperature control system, a circulating pump, a marsh gas reaction tank, wherein an electric heating pipe is equipped with a certain number's in the solar hot water storage tank, an automatic temperature control system comprises a 3 temperature sensor, 6 electromagnetic valves and 1 change the temperature intelligent control instrument, 3 sensors are respectively installed on the water tank, a hot water buffer and the biogas fermenting tank, 6 electromagnetic valves at each upper hot water circulating loop. The utility model can solve northern marsh gas in winter is low and the temperature of the material liquid is not normally ferment gas's and ensures the fermentation device in winter's production rate and high gas concentration, prolongs the use period's marsh gas in winter. At the same time, this utility model also can realize the's hot water in the solar heat collector is directly provided to the user so as to meet the user's demand for hot water in summer.
NOVELTY - Upper connection path one by organic waste hydrogen's device, wherein it comprises an anaerobic fermentation tank (1), connected in series's microbial fuel cell (2), microbial electrolytic cell (3), a current stabilizer (4), wherein said anaerobic fermentation tank (1)'s organic waste water outlet is connected with a microbial fuel cell (2) and electrolytic cell (3), microbial electrolytic cell (3)'s and microbiological fuel cell anode (2)'s anode, microorganism electrolysis cell (3)'s cathode and microbial fuel cell (2) is connected with the cathode's, said microbial fuel cell (2) to the micro-organism electrolytic cell (3), micro-organism electrolytic cell (2) and the fuel cell (3) is equipped with current stabilizer's (4). The utility model uses the MFC-MEC from the power supply system provides the hydrogen's energy, making the organic waste hydrogen in the process reduces the energy consumption, fully recycling and reduce pollution.
NOVELTY - This utility model claims the one using biological enzymolysis's air purifying device, comprising a shell and a fan in the shell, the side wall of the shell's upper wall is provided with an air inlet hole and an exhaust hole, an air inlet hole is located at the exhaust hole, the shell is provided with a cylindrical filter body and biological enzymolysis absorption module's water tank, a cylindrical filter body comprises a horizontal's upper flat plate and a lower flat plate and upper flat plate and a lower flat plate's multiple vertically arranged air's hollow tube, the hollow tube's side wall of air filter screen's loaded with bio-enzyme, and the ventilating pipe is connected with the hollow tube's upper through hole on the upper plate and the lower plate, the upper plate is located between the air inlet hole and an exhaust hole, the lower plate is the air inlet hole, a water tank is located on the lower plate's. The utility model uses biological enzyme to carry out purifying indoor environment, not only can effectively degrade harmful to human body such as formaldehyde's organic matter, but also can play the role's and, it will not cause secondary pollution.
NOVELTY - Addition of microorganism flocculating agent in activated sludge dewatering performance comprises adding activated sludge in sewage treatment plant, purifying and screening, oscillating for 2-3 days, adding fermentation liquid, using freezing ethanol precipitation method to extract flocculating agent, adding microorganism flocculating agent as active sludge sample, magnetically stirring at 400-500 revolutions/minute for 30-60 seconds, and at 100-200 revolutions/minute for 3-6 minute, sludge dewatering and conditioning microorganism flocculating agent.    USE - Method for adding microorganism flocculating agent in active sludge dewatering performance (claimed).    DETAILED DESCRIPTION - Addition of microorganism flocculating agent in activated sludge dewatering performance comprises adding activated sludge in sewage treatment plant, purifying and screening to obtain high active microorganism flocculating agent, at 25-40 degrees C under 100-200 revolutions/minute, oscillating for 2-3 days, adding fermentation liquid under 4000-5000 revolutions/minute for 30 minutes, using freezing ethanol precipitation method to extract flocculating agent from fermentation clear liquid, adding microorganism flocculating agent as active sludge sample, magnetically stirring at 400-500 revolutions/minute for 30-60 seconds, and at 100-200 revolutions/minute for 3-6 minute, sludge dewatering and conditioning microorganism flocculating agent.
NOVELTY - Preparing biodiesel comprises placing the raw oil into the drying room, increasing the temperature of the room with hot air furnace, and obtaining the liquid feedstock; placing the liquid feedstock into a reaction vessel, adding a first enzyme complex catalyst, obtaining liquid A; centrifuging liquid A, discarding supernatant, obtaining liquid B; placing liquid B into a reaction vessel, increasing the temperature of the vessel, and adding a second enzyme complex catalyst.    USE - The method is used for preparing biodiesel (claimed).    ADVANTAGE - The method for preparing biodiesel is rapid, environment-friendly, low cost, highly efficient, non-toxic, simple, and practical, and requires mild reaction conditions.    DETAILED DESCRIPTION - Preparing biodiesel comprises (a) placing the raw oil into the drying room, increasing the temperature of the room with hot air furnace to 145-155 degrees C, and obtaining the liquid feedstock; (b) placing the liquid feedstock into a reaction vessel, adding a first enzyme complex catalyst, obtaining liquid A; (c) centrifuging liquid A at 11000-13000 rounds per minute (rpm) for 30-40 minutes, discarding supernatant, obtaining liquid B; (d) placing liquid B into a reaction vessel, increasing the temperature of the vessel to 68-78 degrees C, adding a second enzyme complex catalyst; (e) centrifuging at 11000-13000 rpm for 80-90 minutes, removing catalyst and residuals, obtaining liquid C; and (f) placing liquid C in a reaction vessel, increasing temperature to 105-115 degrees C, adding 2.5-3.5% bleaching agent, reacting for 28-40 hours, frame filtering and obtaining the biodiesel.
NOVELTY - Microbial composition comprises Bacillus fusiformis, Comamonas sp. and Ochrobactrum sp..    USE - The microbial composition is used as activated sludge for processing wastewater discharged from paper-making industry and enhancing chemical oxygen demand (COD) in the activated sludge (all claimed).    ADVANTAGE - The microbial composition provides effective, rapid and enhanced activated sludge performance, and enables wastewater treatment with high efficiency, and hence improves color and quality of water.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the above-mentioned microbial composition, involves (a) activating the above-mentioned microbial species, inoculating activated microbial strains in liquid medium and performing culturing process at 30 degrees C for 40-54 hours to obtain microbial broth, (b) mixing the microbial broth uniformly, drying the broth at 40-60 degrees C, crushing dried product to 15-50 mesh size sieve, adding and mixing crushed microbial product with solid auxiliary materials uniformly, drying obtained mixture at 40-60 degrees C and crushing obtained mixture to obtain 15-50 mesh size microbial composition, where per 1 l of the microbail broth is added with 1.5 kg solid auxiliary materials; and    (2) use of the above-mentioned microbial composition in combination with activated sludge for processing wastewater discharged from paper-making industry, where the microbial composition and activated sludge are mixed in a weight ratio of 1:1000-1:10000 preferably 1:2000.
NOVELTY - A Bacillus subtilis strain CHS (CGMCC NO. 6128), is new.    USE - The B.subtilis strain CHS and degradation product of 17 beta estradiol are useful for degradation of livestock wastewater (all claimed), and poultry breeding wastewater.    ADVANTAGE - The B.subtilis strain CHS enables degradation of livestock or poultry breeding wastewater in a cost-effective, simple manner with high efficiency, good environment compatibility. The degradation method reduces usage of chemical reagents and hence secondary pollution is also avoided. The method has good application prospects and bioremediation aspects.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing 17 beta estradiol degradation product, which involves inoculating the above-mentioned B.subtilis strain CHS in Luria-Bertani (LB) medium containing ammonia, incubating inocualted medium at 37 degrees C under shaking conditions for 12-36 hours and freeze-drying the medium to obtain 17 beta estradiol degradation product; and (2) degradation product of 17 beta estradiol prepared by the above-mentioned method.
NOVELTY - An Escherichia coli X2 (CCTCC M2013017), is new.    USE - The E.coli X2 is useful for reducing generation of hydrogen sulfide in cattle excrement (all claimed).    ADVANTAGE - The E.coli X2 reduces generation of hydrogen sulfide to 14-40.9% and is environmentally-friendly.
NOVELTY - Method for increasing rate of methanogenesis in a petroleumreservoir comprising methanogenic microbial consortia and foundation water, involves (a) injecting through a well head a solution of stimulants comprisingammoniumions and phosphate ions into the reservoir in an amount such that theirconcentration in atleast a portion of the reservoir is above the critical concentration to effectenhancedmethanogenesis, and (b) maintaining the reservoir under conditions such that the rate ofmethanogenesis is increased.    USE - The method is useful for increasing rate of methanogenesis in a petroleumreservoir comprising methanogenic microbial consortia and foundation water (claimed).    ADVANTAGE - The method stimulates methane production to maximize the potential of subsurface oil reservoirs as sources of hydrocarbons, and enhances total amount of nutrients available to the microbes in a manner such that methane generation is maximized while at the same time ensures that the concentration of nutrients in the reservoir is non-lethal to the microbes.    DETAILED DESCRIPTION - Method for increasing rate of methanogenesis in a petroleumreservoir comprising methanogenic microbial consortia and foundation water, involves (a) injecting through a well head a solution of stimulants comprisingammoniumions and phosphate ions into the reservoir in an amount such that theirconcentration in atleast a portion of the reservoir is above the critical concentration to effectenhancedmethanogenesis but at a non-lethal level to the methanogenic microbialconsortia, and (b) maintaining the reservoir under conditions such that the rate ofmethanogenesis is increased, where the concentration of the ammonium ions injected through the well headis upto about saturation concentration and the concentration of phosphate ionsinjected through thewell head is up to about saturation concentration.
NOVELTY - Enhancing lignin degradation involves fermenting Phanerochaete chrysosporium strain that is used as a starting material. Fermentation is carried out on straw raw material for expanding culture and shaking liquid culture. Primary culture is provided for performing solid fermentation to obtain manganese peroxidase from Phanerochaete chrysosporium strain.    USE - Method for enhancing lignin degradation (claimed).    ADVANTAGE - The method is simple and eco-friendly.
NOVELTY - The product Organic Liquid Formulation of Pseudomonas fluorescens with a CFU of 2x109 ml of product, with a shelf life of 12 months is produced using organic substrates. It helps in the long term establishment of this bio-agent in the soil eco-system or in capsicum and okra crops rhizosphere which is essential for their effective utilization by the crop plants for increasing the productivity and has organic base that can be used for enrichment of vermicompost or any other organic substance. This can be sprayed safely on most of the crops without any toxicity to foliage of crop plants. This can be delivered effectively to root rhizosphere through the irrigation system. This can be used successfully for the growth promotion of crop plants. Application of this product to soil over a period of time can lead to the development of disease suppressive soil and contribute the sustainable crop production.
NOVELTY - Green synthesis of alpha -hydrazino ketones (I) is claimed.    USE - (I) are useful in medicine and pesticide.    ADVANTAGE - The method is economical, free from catalyst and toxic solvents, safe and non-toxic and environmentally friendly.    DETAILED DESCRIPTION - Green synthesis of alpha -hydrazino ketones of formula (I) is claimed.    R1 = ethyl or isopropyl;    R2 = methoxy, ethoxy, phenyl or methyl; and    R3 = methyl, propyl, isopropyl, phenyl, p-nitrophenyl or C7H7O.
NOVELTY - Carfilzomib intermediates, which are (S)-2-amino-N-((S)-3-methyl-1-((R)-(2-methyl-oxiranyl)-oxo-methyl)-butyl)-3-phenyl-propionamide compounds (I) and (S)-2-amino-N-(1-((S)-isobutyl)-3-methyl-2-oxo-but-3-enyl)-3-phenyl-propionamide compounds (II), are new.    USE - (I) and (II) are useful as carfilzomib intermediates (claimed).    ADVANTAGE - The method involves highly selective epoxidation reaction and condensation reaction; is economical, efficient and environmentally friendly; and has short synthesis route, mild reaction conditions, simple operation and high yield and purity.    DETAILED DESCRIPTION - Carfilzomib intermediates, which are (S)-2-amino-N-((S)-3-methyl-1-((R)-(2-methyl-oxiranyl)-oxo-methyl)-butyl)-3-phenyl-propionamide compounds of formula (I) or their salts and (S)-2-amino-N-(1-((S)-isobutyl)-3-methyl-2-oxo-but-3-enyl)-3-phenyl-propionamide compounds of formula (II) or their salts, are new.    R = H or amino protecting group.    INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) preparing carfilzomib, comprising reacting (S)-2-amino-N-((S)-3-methyl-1-((R)-(2-methyl-oxiranyl)-oxo-methyl)-butyl)-3-phenyl-propionamide (representative of (I)) with (S)-4-methyl-2-((S)-2-(2-morpholin-4-yl-acetylamino)-4-phenyl-butyrylamino)-pentanoic acid.
NOVELTY - Manufacturing a biodiesel fuel, comprises: mixing a co-solvent, a first reactant and a second reactant together in a mixing chamber to form a homogeneous solution; and transferring the homogeneous solution into a transesterification reaction vessel. The first and second reactants are substantially immiscible with each other in the absence of the co-solvent. The first reactant is one of an alcohol or oil. The second reactant is the other of the oil or alcohol.    USE - The method is useful for manufacturing a biodiesel fuel.    ADVANTAGE - The method can be carried out by conducting the transesterification reaction at higher temperatures that favorably shift the equilibrium towards the desired biodiesel fuel reaction product, thus enhancing the yield of biodiesel fuel, without the need for spending additional time and energy to separate the alcohol and glycerol.
NOVELTY - Converting biomass to renewable fuels, comprises providing a system containing processing stations in communication with a series of catalysts, heating a biomass within the stations at a starting temperature to produce a volatile and a non-volatile component, where the biomass and the heating step are selected to provide volatile components of a predetermined composition, and subjecting the volatile components of a predetermined composition generated in at least one station through the series of catalysts to produce at least one renewable fuel.    USE - The method is useful for converting biomass (including lipids, hemicellulose, cellulose and lignins) to renewable fuels (all claimed) such as gasoline, jet fuel, diesel and fuel blends (such as a blend of benzene, toluene and xylene) useful for the transportation or other purposes.    ADVANTAGE - The method is capable of efficiently converting biomass to renewable fuels with less energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for converting biomass to combustible fuels, comprising a device containing a programmable number of processing stations and a series of catalysts, a heater for subjecting biomass within the stations to at least one programmable starting temperature, a controller for incrementing an individual processing station temperature by programmable increments to produce a volatile and a non-volatile component, series of catalysts for contacting the volatile components generated in each station to produce at least one renewable fuel, and a processor for receiving data related to one or more of renewable fuel yield or temperature of devolatization of biomass components and determining a sequence of catalyst contacts.
NOVELTY - The device comprises a cylindrical container to accommodate fuel, a swiveling part to control output of combustive air, a support for the container, and a unit for compaction of sawdust. The device allows the combustion of the compacted sawdust. The compaction of the sawdust is carried out by a rotating screw actuating a press. The blocking of the screw in vertical translation is done through a tray in horizontal translation and also allows the tray to accommodate a flammable liquid fuel for the startup of the combustion of sawdust.    USE - The combustion device is useful for cooking, drying or heating food (claimed) in a kitchen for domestic or commercial applications.    ADVANTAGE - The combustion device is simple and safe to use, and has good combustion performance.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic perspective view of a combustion device.    Removable lid (1)    Cylindrical body. (2)
NOVELTY - Soft capsule comprises (a) 0.36-0.46 mg Ginkgo biloba extract as active ingredient containing total flavonol glycoside, and terpene lactone in bilobalide, and (b) 0.09-0.13 mg ginkgolide A, ginkgolide B, and ginkgolide C.    USE - As soft capsule.    ADVANTAGE - The soft capsule has stable property, long storage time, short disintegrating time, and fast dissolution rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the capsule, which involves (a) preparing G.biloba extract powder by crushing G.biloba, adding hemicellulase, L-amino acid oxidase, and phospholipase in weight ratio of 2:6-10:1, mixing mixture, adding 0.3-0.8 times water to the mixture, boiling the mixture for 20 minutes, filtering the mixture, concentrating the mixture at 60 degrees C until relative density of concentrate reaches 1.2, and vacuum drying extract at 80 degrees C to obtain extract powder, (b) preparation of content by mixing the G.biloba extract powder, grape seed oil, and mannitol at 45 degrees C, (c) preparation of glue by adding gelatin to purified water, heating mixture at 35 degrees C, adding remainder raw materials to mixture, and stirring the mixture for 15 minutes, and (d) preparation of finished product by mixing the mixtures obtained in step (b) and (c), and formulating the mixture to capsule.
NOVELTY - A Lamiophlomis rotata soft capsule contains 0.063-0.078 mg rutin component per mg of flavonoid component.    USE - A Lamiophlomis rotata soft capsule (claimed).    ADVANTAGE - Preparation process is low-cost and environment-friendly and has reduced energy consumption.    DETAILED DESCRIPTION - A Lamiophlomis rotata soft capsule contains 0.063-0.078 mg rutin component of formula (C27H30O16) per mg of flavonoid component. An INDEPENDENT CLAIM is included for preparation of Lamiophlomis rotata soft capsule which involves mixing ground L. rotata extract powder, cellulose, D-amino acid oxidase, and phospholipase in which weight ratio cellulose:D-amino acid oxidase:phospholipase is 5-10:10-12:1 and amount of ground L. rotata extract powder is 0.5-0.8 times the amount, adding water into ground mixture and decocting for 25 minutes, filtering, concentrating filtrate at 60 degrees C into clear paste with relative density of 1.2, drying under reduced pressure at 80 degrees C to obtain L. rotata extract powder, mixing L. rotata extract powder, grape seed oil, and mannitol at 50 degrees C, and allowing to stand to obtain mixed components, adding gelatin powder into purified water, heating components to 35 degrees C, adding glycerol, polyethylene glycol 400, bright black, and xylitol, stirring to mix components for 15 minutes, allowing mixed components to stand to obtain gel composition, and subjecting mixed components and gel composition into pellet machine.
NOVELTY - A loaded cerium ammonium sulfate mesoporous biodiesel oil catalyst consists of 5-40 %mass ammonium sulfate as an active component and remaining mesoporous silica carrier. The mesoporous silica has bimodal pore size distribution, mesopores aperture of 3-5 nm and aperture hole of 10-15 nm.    USE - Loaded cerium ammonium sulfate mesoporous biodiesel oil catalyst (claimed).    ADVANTAGE - The biodiesel oil is manufactured at high yield of more than 90% using the catalyst.
NOVELTY - Tea fertilizer and its preparation method are claimed. The tea fertilizer comprises 30 wt.% organic acid, 25 wt.% grass peat, 10 wt.% vegetable protein, 10 wt.% plant activating enzyme, 5 wt.% syrup, 5 wt.% yeast, 5 wt.% jam, 3 wt.% Trichoderma, 3 wt.% Bacillus subtilis, and 3 wt.% B.licheniformis.    USE - As tea fertilizer.    ADVANTAGE - The tea fertilizer enables to increase soil fertility, and improve yield, has disease-resistant ability against insect pest, avoids application of farm chemical and does not leaves residues.    DETAILED DESCRIPTION - Tea fertilizer and its preparation method are claimed. The tea fertilizer comprises 30 wt.% organic acid, 25 wt.% grass peat, 10 wt.% vegetable protein, 10 wt.% plant activating enzyme, 5 wt.% syrup, 5 wt.% yeast, 5 wt.% jam, 3 wt.% Trichoderma, 3 wt.% Bacillus subtilis, and 3 wt.% B.licheniformis. The method involves adding the above-mentioned raw materials into reaction kettle at 40-46 degrees C and stirring speed of 10-12 revolutions/minute, where the water content of the raw material is 55-60%, activating fungi in the mixture by providing enough nutrient for 36 hours, adding biological bacterial fertilizer to the kettle, and covering using black plastic film, performing drying at 45-48 degrees C for 12-36 hours, and maintaining the humidity to 30-35%, and packing the obtained product in bottle or plastic bag.
NOVELTY - Salicylic acid, acetone, and potassium hydroxide are stirred at room temperature. Bromoethane is dripped, and the mixture is heat-refluxed for 9-15 hours, decompressed, and filtered to recycle acetone. Water and liquid alkali are added, and the reaction mixture is heat-refluxed for 2-4 hours, cooled to room temperature, pH-adjusted to 3-4, cooled to 1-15 degrees C, and filtered. The separated residue is water-washed and vacuum-dried to obtain o-ethoxybenzoic acid. The ratio of salicylic acid, potassium hydroxide, bromoethane, and liquid alkali is 1:2:2.1:1.4.    USE - Synthesis of o-ethoxybenzoic acid (claimed).    ADVANTAGE - The method enables simple and convenient industrial synthesis of o-ethoxybenzoic acid with high yield and quality, using economical raw materials.
NOVELTY - Salicylic acid, acetone, and potassium hydroxide are stirred at room temperature. Bromoethane is dripped, and the mixture is heat-refluxed for 9-15 hours, decompressed, and filtered to recycle acetone. Water and liquid alkali are added, and the reaction mixture is heat-refluxed for 2-4 hours, cooled to room temperature, pH-adjusted to 3-4, cooled to 1-15 degrees C, and filtered. The separated residue is water-washed and vacuum-dried to obtain o-ethoxybenzoic acid. The ratio of salicylic acid, potassium hydroxide, bromoethane, and liquid alkali is 1:2.3:2.3:1.3.    USE - Synthesis of o-ethoxybenzoic acid (claimed).    ADVANTAGE - The method enables simple and convenient industrial synthesis of o-ethoxybenzoic acid with high yield and quality, using economical raw materials.
NOVELTY - Salicylic acid, acetone, and potassium hydroxide are stirred at room temperature. Bromoethane is dripped, and the mixture is heat-refluxed for 9-15 hours, decompressed, and filtered to recycle acetone. Water and liquid alkali are added, and the reaction mixture is heat-refluxed for 2-4 hours, cooled to room temperature, pH-adjusted to 3-4, cooled to 1-15 degrees C, and filtered. The separated residue is water-washed and vacuum-dried to obtain o-ethoxybenzoic acid. The ratio of salicylic acid, potassium hydroxide, bromoethane, and liquid alkali is 1:2.5:2.5:1.5.    USE - Synthesis of o-ethoxybenzoic acid (claimed).    ADVANTAGE - The method enables simple and convenient industrial synthesis of o-ethoxybenzoic acid with high yield and quality, using economical raw materials.
NOVELTY - Processing of barbecue charcoal involves mixing 100 pts. wt. combustible crop waste, 20-30 pts. wt. combustion improver, 10-20 pts. wt. binder and 100 pts. wt. water, molding the obtained paste in compression molding machine, and drying.    USE - Processing of barbecue charcoal (claimed).    ADVANTAGE - The lightweight barbecue charcoal is economically and environmentally-friendly processed by simple process without generation of smoke and odor, under reduced energy consumption.
NOVELTY - A resin composition contains 0.1-5 mass parts carbodiimide compound (B) and 0.01-0.5 mass part antioxidant and 100 mass parts polyarylate resin (A).    USE - A resin composition for biodiesel fuel containers and molded object used as filter container for biodiesel fuel (all claimed).    ADVANTAGE - Polyarylate resin composition maintains the heat resistance and mechanical characteristics of the conventional polyarylate resin and has sufficient moldability and sufficient tolerance with respect to biodiesel fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for molded object which is formed by molding resin composition for biodiesel fuel containers.
NOVELTY - Special fertilizer for tea tree comprises raw materials comprising urea, waste wine lees, mushroom residue, animal urine, excrementum bombycis, cabbage, corn flour, ammonium polyphosphate, sodium tartrate, EDTA, zinc sulfate heptahydrate, monohydrate manganese sulfate, jade powder, castor leaves powder, bitter wormwood powder, color-leafed grass powder, pepper powder and modified loess.    USE - The special fertilizer is useful for tea tree (claimed).    ADVANTAGE - The special fertilizer meets need of different growth periods and diseases and insect pests, reduces time, and improves quality of soil and trees.    DETAILED DESCRIPTION - Special fertilizer for tea tree comprises raw materials comprising 16-20 pts. wt. urea, 35-40 pts. wt. waste wine lees, 8-10 pts. wt. mushroom residue, 15-20 pts. wt. animal urine, 12-15 pts. wt. excrementum bombycis, 12-15 pts. wt. cabbage, 1-3 pts. wt. corn flour, 2-3 pts. wt. ammonium polyphosphate, 4-6 pts. wt. sodium tartrate, 2-4 pts. wt. EDTA, 1-3 pts. wt. zinc sulfate heptahydrate, 2-4 pts. wt. monohydrate manganese sulfate, 3.5-4.5 pts. wt. jade powder, 3-5 pts. wt. castor leaves powder, 2-4 pts. wt. bitter wormwood powder, 1-2 pts. wt. color-leafed grass powder, 2-3 pts. wt. pepper powder and 5-8 pts. wt. modified loess. An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing 100-120 pts. wt. loess, 30-40 pts. wt. plant ash, 10-12 pts. wt. soybean oil, 10-12 pts. wt. starch, 1-2 pts. wt. sodium dodecyl benzene sulfonate, 0.2-0.3 pts. wt. zinc gluconate powder and water, mixing raw materials for 2-3 hours, milling powder at 460-480 degrees C, adding starch and sodium dodecyl benzene sulfonic acid sodium salt into water, heating mixture, adding calcined loess powder, plant ash, zinc gluconate powder and soybean oil, mixing and stirring for 40-50 minutes, drying mixture at 60-70 degrees C, and crushing into coarse granule size of l-3 mm.
NOVELTY - Fertilizer comprises dry pig manure, kelp slag, pomegranate powder, bamboo charcoal powder, alum powder, bentonite, polyvinyl alcohol, borax, soybean oil, jade nanopowder, alginic acid propylene glycol ester, sodium selenite, manganese sulfate, ferrous sulfate, ammonium citrate, chinaberry bark, Salvinia natans, Perilla, Pedicularis, and Centella asiatica.    USE - The fertilizer is useful for jujube tree.    ADVANTAGE - The fertilizer can be effectively absorbed by the plant, and reduces the poisonous heavy metal element in the soil.    DETAILED DESCRIPTION - Fertilizer comprises 30-35 pts. wt. of dry pig manure, 16-20 pts. wt. of kelp slag, 3-5 pts. wt. of pomegranate powder, 6-8 pts. wt. of bamboo charcoal powder, 20-25 pts. wt. of alum powder, 40-50 pts. wt. of bentonite, 2-4 pts. wt. of polyvinyl alcohol, 1-3 pts. wt. of borax, 5-8 pts. wt. of soybean oil, 4-6 pts. wt. of jade nanopowder, 1-2 pts. wt. of alginic acid propylene glycol ester, 1-2 pts. wt. of sodium selenite, 2.5-3.5 pts. wt. of manganese sulfate, 1-2 pts. wt. of ferrous sulfate, 0.5-1.5 pts. wt. of ammonium citrate, 2-3 pts. wt. of chinaberry bark, 4-6 pts. wt. of Salvinia natans, 2-4 pts. wt. of Perilla, 5-6 pts. wt. of Pedicularis, and 3-5 pts. wt. of Centella asiatica. An INDEPENDENT CLAIM is included for preparing the fertilizer comprising pouring the above raw materials, crushing into fine powder, uniformly stirring for 1-2 hours, wrapping the sludge and standing for 15-20 days, heating at 25-40 degrees C, uniformly stirring and stacking the sludge and fermenting for 5-10 days.
NOVELTY - Invention relates to chemistry. According to the first version, hydrogen is produced by insulating iron rods from walls of a reactor 1 and applying high-voltage potential from a Tesla coil 14 across said rods. The reactor 1 is earthed and filled with water until a discharge forms between iron electrodes and the surface of the water. According to the second version, a flat horizontal cooled electrode 18 is insulated from walls of the reactor 1 and high-voltage potential from a Tesla coil 14 is applied across said electrode. The reactor is earthed. Thin-walled tubes 23 made of iron with a displacement device 24 are mounted vertically inside the reactor. The distance between the thin-walled tubes and the flat electrode 18 is reduced until a discharge forms. Water vapour is fed through the thin-walled tubes.    USE - Chemistry.    ADVANTAGE - Invention increases purity of hydrogen and reduces power consumption.6 cl, 2 dwg, 2 ex
NOVELTY - The method involves separating the first gas including methane and second gas including carbon dioxide using gas purification separate unit (100). The fuel anode gas is supplied to the fuel anode (410) of molten carbonate fuel cell (400) using fuel anode gas supply unit (200). The air electrode gas is supplied to the air electrode (420) of fuel cell through air electrode gas supply unit (300).    USE - Method for supplying biogas to molten carbonate fuel cell system (claimed).    ADVANTAGE - The separation of methane and carbon dioxide is possible, so that the influence of the sulfur about the fuel anode can be minimized. Thus the thermal flow stability due to the pure water supply to the fuel anode can be improved and the voltage rise effect of the battery can be improved. The size of the fuel cell system can be reduced. The natural gas can supply the fuel anode for the stable fuel supply through the mixing portion, so that the stability and availability ratio of the stack can be improved. The catalyst oxidizer from the sulfur compound contained in the carbon dioxide can be reused.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for molten carbonate fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system. (Drawing includes non-English language text)    Gas purification separate unit (100)    Fuel anode gas supply unit (200)    Air electrode gas supply unit (300)    Molten carbonate fuel cell (400)    Fuel anode (410)    Air electrode (420)
NOVELTY - Microbial production of xylitol from xylose containing biomass comprises: (a) growing of yeast strain in a solid medium; (b) inoculating the yeast strain obtained from step (a) in a seed medium containing seed fermentor; (c) culturing the yeast strain by transferring in production fermentor having xylose containing production medium; where fermentation of the xylose containing biomass is carried out with yeast strain capable of converting xylose to xylitol; and (d) removing the yeast strain from the production medium and recycling it for continuous production of xylitol.    USE - The process is useful for microbial production of xylitol from xylose containing biomass (claimed).    ADVANTAGE - The process uses high initial xylose concentration for higher xylitol production in an effectively shorter conversion time. Also, the process is cost-efficient, economical and has high yield.
NOVELTY - The method comprises introducing a food waste into a hopper and then crushing the waste into predetermined size, performing solid-liquid separation on the waste, removing salt from the waste by washing, further removing solid carbide in the waste, drying the waste using a drying unit, preparing a fuel using the dried waste, and supplying air to the waste and then removing odors present in the waste.    USE - The method is useful for solidifying food waste (claimed).    ADVANTAGE - The method is capable of simply and economically solidifying the food waste with less steps and without bad smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for solidifying food waste.
NOVELTY - Air-lift type combined photobioreactor for production of biomass comprises a vertical cylindrical body (30-600 cm in height and 5-70 cm in diameter), a pH meter with temperature compensation, an outlet duct of the crop, an inlet conduit adapted for gas flow gas, a conduit connecting the outlet of cultivation, the gas inlet conduit entry and internal recirculation and a lid, where internal recirculation conduit is located at the bottom comprising an outlet of the internal recirculation and an inlet duct allowing internal recirculation to combine the air-lift effect and bubble column.    USE - The photobioreactor is useful for production of biomass (claimed).    ADVANTAGE - The photobioreactor provides a more efficient stirring; avoids deposition of microalgae; transfers to better light for cultivation; and provides better use of carbon dioxide (CO2).
NOVELTY - The system has fuel generation element (1) that generates a fuel gas by a chemical reaction. Fuel cell (2) generates power using fuel gas supplied from fuel generation element. Gas flow path circulates gas between fuel generation element and fuel cell. Circulator is provided in gas flow path for forcedly circulating the gas between the fuel generation element and the fuel cell. Circulator control unit is set to control the amount of gas circulated by circulator based on percentage of non-chemical reaction in the fuel generation element.    USE - Fuel cell system such as secondary type fuel cell system and domestic fuel cell cogeneration system.    ADVANTAGE - The fuel cell system featured with high-energy efficiency and the stable electric power generation is provided. As the amount of gas circulated by circulator based on percentage of non-chemical reaction in the fuel generation element, the consumption of useless energy by the drive of a circulating system, the short electric power generation amount of fuel cell, and insufficient amount of gas circulation of circulating system can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell system. (Drawing includes non-English language text)    Fuel generation element (1)    Fuel cell (2)    Heater (3)    Container (6)    Piping (7)
NOVELTY - Device comprises an inlet device (1) for introducing the biomass into the device, a hollow shaft (3) with a conveying device for conveying the biomass through the hollow shaft into an upper part of the device, torrefaction floors outside the hollow shaft which allow the biomass to fall downwards from the upper part, and a flue gas supply line (11) for feeding flue gas, such that the biomass is torrefied by the flue gas during transport into the upper part of the device and/or during dropping through the torrefaction floors.    USE - The device is useful for torrifying biomass (claimed).    ADVANTAGE - The device: has simple construction; exhibits reduced energy consumption and reduced exhaust gas emission, thus it is environmental friendly.    DESCRIPTION OF DRAWING(S) - The device shows a schematic representation of the device.    Inlet device (1)    Torrefaction tower (2)    Hollow shaft (3)    Bucket conveyor (5)    Flue gas supply line (11)
NOVELTY - Slow-release fertilizer comprises two layer, where the first coating layer and the second coating layer are orderly coated with particle fertilizer, the first coating layer and the second coating layer are hydrophobic modified layer.    USE - Slow-release fertilizer.    ADVANTAGE - The slow-release fertilizer can be prepared simply, is highly stable and nutritious and cost-effective, has controlled-release property, and enables to completely biodegrade the wrapping material without changing the soil environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing slow-release fertilizer, which involves placing the fertilizer in a stirring device, stirring the material at 100-3000 rotations/minute in presence of modifier, starch and molasses, coating the mixture on first coating layer, drying, then coating subhydrophobic modifier on the second coating layer, drying and obtaining the product.
NOVELTY - Catalytic oxidation of organic alcohol with molecular oxygen comprises mixing organic alcohol, composite catalyst and organic solvent or de-ionized water; and stirring uniformly to obtain reaction system, reacting at 0.002-5 MPa in the presence of oxygen or air at 50-240 degrees C for 0.5-10 hours. The composite catalyst comprises 2,3-dichloro-5,6-dicyano-p-benzoquinone, sodium nitrite and halo-succinimide.    USE - Method for catalytic oxidation of organic alcohol with molecular oxygen to prepare aldehyde or ketone (claimed).    ADVANTAGE - The method uses composite catalyst having low cost and that is easy to obtain. The catalyst further has high efficiency and high selectivity. The reaction by-product is water, providing less pollution and making the method environment-friendly.
NOVELTY - Propionic acid is added to chlorination reactor, sealed, heated, red phosphorus is added, chlorine is added, pressurized, incubated and cooled, to obtain 2-chloro-propionic acid. The obtained product is added to reactor, sealed, hexamethylenetetramine is added, reacted, ammonia is added and stirred, to obtain 2-aminopropanoic acid. The obtained product is added to crystallization reactor, methanol is added, stirred for 30 minutes, allowed to stand, centrifuged, solid-liquid separation is performed, vacuum-dried, crushed, sieved and packed, to obtain alanine.    USE - Manufacture of alanine (claimed).    ADVANTAGE - The method efficiently provides alanine with high yield and suppressed waste generation by economical process.    DETAILED DESCRIPTION - 18-20 wt.% Propionic acid is added to chlorination reactor, sealed, heated to 102-104 degrees C under stirring condition, 1 wt.% red phosphorus is added, 19-21 wt.% chlorine is added, pressurized, pressure is adjusted to 0.4 MPa, incubated for 2-2.4 hours, stirring is terminated and cooled to 65 degrees C, to obtain 2-chloro-propionic acid. The obtained product is added to reactor, sealed, reaction temperature is controlled to 56-58 degrees C, 2 wt.% hexamethylenetetramine is added under stirring condition, reacted for 5 minutes, 58 wt.% ammonia is added and stirred for 3-3.2 hours, to obtain 2-aminopropanoic acid. The obtained product is added to crystallization reactor, 2-3 times methanol is added, stirred for 30 minutes, allowed to stand for 24 hours, centrifuged, solid-liquid separation is performed, vacuum-dried, dried at 75-85 degrees C for 11-13 hours, crushed, sieved and packed, to obtain alanine.
NOVELTY - Ceftriaxone sodium is obtained by reacting (6R,7R)-3-acetoxymethyl-7-amino-8-oxo-5-thia-1-aza-bicyclo(4.2.0)oct-2-ene-2-carboxylic acid and 6-hydroxy-3-mercapto-2-methyl-2H-(1,2,4)triazin-5-one in dimethyl carbonate to obtain 7-amino-3-((2,5-dihydro-6-hydroxy-2-methyl-5-oxo-1,2,4-triazin-2-yl)thiomethyl)cephalosporanic acid (7-ACT), and reacting 7-ACT and (2-amino-thiazol-4-yl)-((Z)-methoxyimino)-thioacetic acid S-benzothiazol-2-yl ester (AE-active ester) in a binary system of ethanol and water.    USE - Preparation of ceftriaxone sodium (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of ceftriaxone sodium, without using expensive and toxic reagents, with high yield and quality.
NOVELTY - Cone or dome-shaped inflatable roof (2) for biogas tank (1), comprises gas-tight and liquid-tight outer film (4) comprising a container mantle with circular or angular basic form on open top of outer wall of tank and heat protection film underneath the outer film, where cone is gastight and comprises in edge area a variety of fermentation gas passage apertures.    USE - The roof is useful for biogas tank.    ADVANTAGE - The roof solves significantly unwanted cooling of the substrate, and drops energy required to stabilize an optimal substrate temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) biogas passage openings reinforced by chain together with yarn, or by introducing passage rivets from plastic or light metal, or by welding on a reinforcement ring made from the same plastic material as the insulation film;    (2) the biogas tank with cone or dome shaped carrying air roof; and    (3) thermic protection film for biogas tank comprising gas-tight with variety of fermentation gas passage apertures in the edge area.    DESCRIPTION OF DRAWING(S) - The figure illustrates schematic side view of the biogas tank.    Biogas tank (1)    Inflatable roof (2)    Top surface (3)    Shell (3a)    Outer film (4)
NOVELTY - Method of reducing pollutants and/or toxins in an environment, involves introducing to a contaminated environment an amide-functionalized ordered mesoporus carbon, where the amide-functionalized ordered mesoporus carbon has at least one toxin-degrading enzyme conjugated to the surface.    USE - The method is useful for reducing pollutants and/or toxins in environment (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofilter, which comprises a porous material and an amide-functionalized ordered mesoporus carbon, where the amide-functionalized ordered mesoporus carbon has at least one toxin-degrading enzyme conjugated to the surface.
NOVELTY - Artificial soil containing organic sludge comprises fermented manure, coco peat, zeolite, vermiculite and red clay.    USE - The artificial soil is useful for three-dimensional greening (claimed) and as compost for plant growth.    ADVANTAGE - The artificial soil utilizes and recycles organic waste generated from the food factory.
NOVELTY - Biochar is obtained by performing pyrolysis of organic waste material at 500 degrees C for 2 hours and 5 minutes.    USE - The biochar is useful for increasing uptake of nitrogen by plants (claimed).    ADVANTAGE - The biochar improves efficiency of nitrogen fertilizer, and maintains stability of biomass production in maize crop.
NOVELTY - Medium comprises micropore structure.    USE - The medium is useful for promoting activity of environmental microorganisms, and in fermentation and disposal of active sludge in food waste, dirty water, sewage or wastewater or livestock sludge.    ADVANTAGE - The medium significantly reduces weight of by-product or sludge, when filth is fermented and disposed using the medium, and generates less offensive odor during fermentation and disposal, and has excellent durability, and hence it can be used over a long period of time, and is suitable for inhabitation of microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned medium, which involves treating plant-based biomass (raw material) with base, where the medium has the capability to promote activity of environmental microorganisms.
NOVELTY - Parasol tree fertilizer comprises 23-25 pts. wt. of human and animal urine, 18-20 pts. wt. of biogas fertilizer, 10-12 pts. wt. of grape wine powder, 10-15 pts. wt. peanut leaves, 30-40 pts. wt. of nano-iron slag powder, 4-6 pts. wt. of corn flour, 2-4 pts. wt. of seaweed powder, 1-3 pts. wt. of carboxymethyl cellulose, 5-7 pts. wt. of modified clay powder, 4-5 pts. wt. of sodium selenite, 1-2 pts. wt. of potassium sulfate, 1-3 pts. wt. of potassium chloride, 2-4 pts. wt. of zinc sulfate, 1-3 pts. wt. of phosphorus pentoxide, 0.5-0.8 pts. wt. of manganese sulfate, and 1-2 pts. wt. of borate.    USE - Parasol tree fertilizer.    ADVANTAGE - The parasol tree fertilizer improves the quality of the soil in a rapid manner.    DETAILED DESCRIPTION - Parasol tree fertilizer comprises 23-25 pts. wt. of human and animal urine, 18-20 pts. wt. of biogas fertilizer, 10-12 pts. wt. of grape wine powder, 10-15 pts. wt. peanut leaves, 30-40 pts. wt. of nano-iron slag powder, 4-6 pts. wt. of corn flour, 2-4 pts. wt. of seaweed powder, 1-3 pts. wt. of carboxymethyl cellulose, 5-7 pts. wt. of modified clay powder, 4-5 pts. wt. of sodium selenite, 1-2 pts. wt. of potassium sulfate, 1-3 pts. wt. of potassium chloride, 2-4 pts. wt. of zinc sulfate, 1-3 pts. wt. of phosphorus pentoxide, 0.5-0.8 pts. wt. of manganese sulfate, 1-2 pts. wt. of borate, 2-4 pts. wt. of pine needle powder, 3-5 pts. wt. of Trachelospermum, 2-4 pts. wt. of Rhaponticum uniflorum, 1-3 pts. wt. of Typhonium giganteum, and 10-12 pts. wt. of orange cake. An INDEPENDENT CLAIM is included for a method for preparing a parasol tree fertilizer comprising mixing human and animal urine, pine needle powder, Trachelospermum, Typhonium giganteum and orange cake, adding 0.1-0.3 wt.% of microorganism agent to the mixture, fermenting the mixture for 10-15 days, and granulating and drying the mixture to obtain a product.
NOVELTY - Micro-nanoparticle comprises resveratrol and carrier material chosen from polylactic acid-glycolic acid copolymer, where the mass ratio of polylactic acid-glycolic acid copolymer and resveratrol is 1:0.1-1.    USE - The micro-nanoparticle comprising resveratrol is useful in pharmaceuticals.    ADVANTAGE - The micro-nanoparticle can be prepared simply and rapidly with less energy consumption, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing micro-nanoparticle, which involves completely dissolving polylactic acid-glycolic acid copolymer in a mixed solvent of tetrahydrofuran and acetone, adding resveratrol and distilled water under stirring, rapidly volatilizing the organic solvent, then using deionized water removing free resveratrol, centrifuging the solution, removing supernatant, collecting precipitate and drying to obtain the product.
NOVELTY - Processing sludge comprises mixing antidote with wet municipal sludge, then drying, or mixing antidote with dry municipal sludge, where the moisture content of the mixture is not more than 15%, the antidote accounts for 3-20 wt.% of dry municipal sludge; (ii) pulverizing the obtained mixture, and sieving to obtain cracking raw material; (iii) adding the cracking raw material into carbonization oven and carrying out low temperature limited oxygen pyrolysis, and cooling, where the pyrolysis temperature is 280-420 degrees C, pyrolysis time is 40-120 minutes, and using nitrogen as protective gas.    USE - The sludge biochar is useful for agricultural (claimed).    ADVANTAGE - The method reduces total amount of active heavy metals and carbonized product, kills bacteria, removes polycyclic aromatic hydrocarbon and organic pollutant, but retains nutrient product suitable for agriculture and forestry and farming field.    DETAILED DESCRIPTION - Processing sludge comprises (i) mixing antidote with wet municipal sludge, then drying, or mixing antidote with dry municipal sludge, where the moisture content of the mixture is not more than 15%, the antidote accounts for 3-20 wt.% of dry municipal sludge, the antidote is organic and/or inorganic antidote, where the organic antidote us a lignin, humic acid and/or monosodium glutamate factory scraps and wastes, and the inorganic antidote is fly ash, phosphogypsum, diatomaceous earth, calcium sulfate and/or magnesium; (ii) pulverizing the obtained mixture, and sieving to obtain cracking raw material; (iii) adding the cracking raw material into carbonization oven and carrying out low temperature limited oxygen pyrolysis, and cooling, where the pyrolysis temperature is 280-420 degrees C, pyrolysis time is 40-120 minutes, and using nitrogen as protective gas.
NOVELTY - An azadirachtin bio-organic fertilizer comprises 15-18 wt.% neem cake, 15-80 wt.% organic compound, and 0.1-5 pts. wt. microbial inoculants.    USE - An azadirachtin bio-organic fertilizer.    ADVANTAGE - The fertilizer is safe and reliable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of azadirachtin bio-organic fertilizer comprising:    (A) cold pressing the neem cake and organic compound, and mixing uniformly to obtain the mixture;    (B) fermenting the mixture, drying and processing, and    (C) adding the microbial agent into the mixture, mixing uniformly, crushing or granulating, detecting and packaging.
NOVELTY - A seaweed extract chelated trace element fertilizer applied as Foliar application comprises 50-80 wt.% fermented amino acid, 1-1.5 wt.% sodium alginate, 2-3 wt.% mannitol, 1-3 wt.% EDTA-copper complex, 10-15 wt.% EDTA-manganese complex, 1-2 wt.% auxiliary agent and balance water.    USE - Seaweed extract chelated trace element fertilizer used for tomato, cucumber and rice.    ADVANTAGE - The fertilizer is rich in amino acid and has high product yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for seaweed extract chelated trace element fertilizer applied as Foliar applicationcomprising mixing sodium alginate and water, reacting at 20-50 degrees C, stirring uniformly, adding fermented amino acid, stirring uniformly, adding EDTA-copper complex, stirring uniformly, adding EDTA-manganese complex, stirring uniformly, adding mannitol, stirring uniformly, adding auxiliary agent, and stirring uniformly.
NOVELTY - An organic fertilizer comprises exchange resin, red bean, crown flower, cow manure, straw powder, phosphate and potassium solubilizing bacteria, polyvinyl alcohol and fermenting bacteria.    USE - Organic fertilizer used for neutralizing cationic soil.    ADVANTAGE - The method is simple. The fertilizer reduces salt content of soil, enhances soil activity of microorganism and enzyme, and promotes plant root system growth. It has improved saline-alkali effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer comprising mixing red bean, crown flower and straw powder, crushing cow manure, uniformly stirring, adding fermenting bacteria, composting at 30-50 cm height, covering with plastic film cover, fermenting for 10-12 days, adding cation exchange resin, phosphate and potassium solubilizing bacteria and polyvinyl alcohol, adding water until 63-65 vol.% water content, extruding, and drying.
NOVELTY - A straw mushroom cultivation base material comprises 50-60 pts. wt. white rice sheath leaf, 18-28 pts. wt. cottonseed hulls, 15 pts. wt. cow manure, 5 pts. wt. lime and 2 pts. wt. gypsum powder.    USE - Straw mushroom cultivation base material.    ADVANTAGE - The cultivation base material has good ventilation. It has 26.7-30.4% biological efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of straw mushroom cultivation base material comprising soaking white rice sheath leaf for 30-36 hours, adding 100 kg water and 5 kg lime, stacking, crushing cow manure, adding 100 kg cow manure, piling at 1.4-1.5 meters height and 2 meters width, fermenting for 15-18 days, adding lime, gypsum powder, and cottonseed hulls, adjusting to 7.5-8 pH, adding lime water, and stopping fermentation until 60-62 vol.% water content.
NOVELTY - A seedling substrate comprises 7-9:1-3 mass ratio of biocontrol fungus and soil.    USE - Seedling substrate used for preventing and curing soil-borne disease (claimed).    ADVANTAGE - The seedling substrate is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for seedling substrate comprising adjusting water content to 40-60 vol.% and pH to 7-8, adding 1-4 vol.% urea, piling, fermenting at 25-30 degrees C, adding biocontrol fungus, reacting under nitrogen atmosphere, fermenting at 40-50 degrees C for 18-30 days, and culturing.
NOVELTY - An epigallocatechin gallate is prepared by dissolving tea polyphenol and purified water, standing, filtering, removing residue, adding organic solvent, extracting, decompressing, concentrating filtrate, adding purified water, pouring tea polyphenol sample solution to macroporous adsorption resin column, eluting, decompressing, concentrating filtrate, dissolving in proper solvent, cooling, crystal seeding, standing, crystallizing, filtering, purifying, and drying.    USE - Method for preparing epigallocatechin gallate (claimed).    ADVANTAGE - The method has low cost, high yield of pure product, environment-friendly effect, and short production period.
NOVELTY - Preparation of nicosulfuron comprises reacting 2-aminosulfonyl-N,N-dimethylnicotinamide, sodium thiocyanate, organic solvent and organic base, stirring at 10-50 degrees C for 2-10 hours, adding 2-amino-4,6-dimethoxypyrimidine, stirring for 0.5-5 hours, and adding 2-amino-4,6-dimethoxypyrimidine.    USE - Method for preparing nicosulfuron (claimed) used as a herbicide.    ADVANTAGE - The method has low cost, high yield of highly pure product, short reaction period, environment-friendly effect and is suitable for industrial production.
NOVELTY - An ertapenem sodium is prepared by mixing phosphorus-containing bicyclo(3,2,0)hept-2-en-6-one derivative (i) and aniline-containing benzoic acid derivative (ii), reacting with palladium on activated charcoal as catalyst and aqueous sodium bicarbonate as alkaline agent, and hydrogenating.    USE - Method for preparing ertapenem sodium (claimed).    ADVANTAGE - The method is simple and environmental-friendly. It reduces costs.
NOVELTY - An ellagic acid from blackberry pomace is prepared by extracting blackberry pomace with 40-80 vol.% alcohol, adding alkaline solution to 11-13 pH, extracting ultrasonically for 1 hour, leaching for 12-24 hours, filtering, adding acid to 2.5-3.5 pH, washing with polyamide resin, water and alkaline solution, cooling at 4 degrees C for 24-48 hours, and centrifuging.    USE - Method for preparing ellagic acid from blackberry pomace (claimed).    ADVANTAGE - The method is simple, environment-friendly and low cost. The product has 60% purity.
NOVELTY - A bilobalide is prepared by extracting Ginkgo biloba extract with organic solvent, evaporating under reduced pressure, performing reversed-phase column chromatography with macroporous adsorption resins, extracting with 0-20 wt.% ethanol and 20-50 wt.% ethanol, recycling elution solvent, drying, dissolving, filtering, cooling at 2-10 degrees C for 12-48 hours, precipitating, crystallizing for 1-3 times, washing for 1-5 times, and vacuum drying at 60-120 degrees C.    USE - Method for preparing bilobalide (claimed).    ADVANTAGE - The method is simple, safe, environment-friendly and is suitable for industrial production; it conserves energy. The product has 98-99%purity.
NOVELTY - Rutin preparation involves taking Sophora flower bud, crushing Sophora flower bud, and adding methanol to the crushed material, where solvent is added to the mixture adjusting the pH value. The mixture is refluxed for 1.5-3 hours. The refluxed mixture is filtered to obtain Sophora flower bud residue. Methanol and mixed solvent are added to the Sophora flower bud residue for adjusting the pH value to 3. Calcium salt is added to the Sophora flower bud residue.    USE - Method for preparing rutin.    ADVANTAGE - The method enables effectively improving purity and yield rutin, and reduces the pollution.    DETAILED DESCRIPTION - Rutin preparation involves taking Sophora flower bud, crushing Sophora flower bud, and adding methanol to the crushed material, where solvent is added to the mixture adjusting the pH value. The mixture is refluxed for 1.5-3 hours. The refluxed mixture is filtered to obtain Sophora flower bud residue. Methanol and mixed solvent are added to the Sophora flower bud residue for adjusting the pH value to 3. Calcium salt is added to the Sophora flower bud residue. The mixture is refluxed for 1-3 hours. The refluxed mixture is filtered to obtain filtrate. The filtrate is washed water. An acid is added to the filtrate for adjusting pH value to 3.5-4. The filtrate is crystallized for 1-4 hours. The crystallized material is washed, centrifuged and crushed, and then methanol is added to the crushed material. The mixture is pulped, centrifuged, dried and crushed to obtain the desired product.
NOVELTY - Biodiesel oil preparation by field induced eutectic system involves refluxing sodium hydroxide as catalyst, choline chloride a eutectic solvent, vegetable oil, which is made of fatty acids and glycerol in methanol solvent by heating for 2-6 hours. The obtained reaction mixture is cooled at room temperature to form a liquid-liquid biphasic system, where upper layer is crude product and lower layer is the eutectic mixture. The obtained crude product is separated, washed and then dried to obtain the biodiesel oil product.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method enables to produce pure biodiesel oil that is cost effective, eco-friendly and easy to recycle.    DETAILED DESCRIPTION - Biodiesel oil preparation by field induced eutectic system involves refluxing sodium hydroxide as catalyst, choline chloride a eutectic solvent, vegetable oil of formula (I), which is made of fatty acids and glycerol of formula (II) in methanol solvent by heating for 2-6 hours. The obtained reaction mixture is cooled at room temperature to form a liquid-liquid biphasic system, where upper layer is crude product and lower layer is the eutectic mixture. The obtained crude product is separated, washed and then dried to obtain the biodiesel oil of formula (III) product. The lower layer of the eutectic mixture containing un-reacted raw materials i.e. catalyst and glycerol are recycled and repeatedly used for preparing biodiesel oil..
NOVELTY - For the preparation of aspartic acid, maleic anhydride waste residue is used.    USE - For the preparation of aspartic acid (claimed).    ADVANTAGE - The maleic anhydride waste residue provides simple, controllable and low cost preparation of aspartic acid; reduces the discharge waste; provides aspartic acid having purity of more than 99.5 wt.%; and provides social environment protection and economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of aspartic acid by using maleic anhydride waste residue as raw material involving a) dissolving the maleic anhydride waste residue into water, heating, filtering undissolved substance to obtain the maleic anhydride waste residue water solution; b) adding maleic anhydride waste residue water solution obtained in step a) into thiourea and maleic acid, heating, reflowing and reacting, where the maleic acid contained in the waste is converted to fumaric acid, after the reaction is finished, cooling and crystallizing, filtering the crystal to obtain fumaric acid-rich crystals; c) adding fumaric acid-rich crystals obtained in the step b) into water, heating, dissolving, adding Escherichia coli and ammonia water, after the reaction, adjusting the pH to less than 6, cooling, crystallizing and filtering to obtain aspartic acid crystal; and d) soaking aspartic acid crystal obtained in step c) in lower alcohol and then washing for removing impurities to obtain aspartic acid crystal (purity more than 99.5 wt.%).
NOVELTY - Formula raw materials comprises 10 kg rabbit dung and rice bran and tofu soybean varieties Grobogan (70%), EM4 (RTM: Mixture of yeast, fungi and bacteria) (30%), molasses that has been mixed with water.    USE - The formula raw materials are useful in fermentation process for making Bokashi express fertilizer (all claimed).    ADVANTAGE - The formula raw materials are safe to environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for Bokashi express fertilizer that contain bioactive compounds in the form of isoflavone glycosides found in soybeans varieties Grobogan preferably in the skin part.
NOVELTY - Fermentation of sludge comprises taking 4 tons of sludge, controlling water content at 60-65%; mixing 1 kg fermenting agent and sludge, stirring uniformly, adding 20-30% straw, mushroom residue, peanut shell powder, rice husk and saw dust; performing aerobic fermentation at 15-20 degrees C for 48 hours, then at 50-60 degrees C and on third day at 75 degrees C; stabilizing at 55-65 degrees C, fermenting for 10-15 days; and drying fermented materials, crushing, pulverizing, sieving and packaging.    USE - Method for fermenting sludge used as organic fertilizer (claimed).
NOVELTY - Preparation of livestock and poultry manure biological organic fertilizer comprises preparing chicken manure and additive; dividing chicken manure; adding strain, performing two-stage fermentation; and drying crushing, sieving, and packaging.    USE - Method for preparing livestock and poultry manure biological organic fertilizer (claimed) used for improving quality crop yield and crop immunity.    DETAILED DESCRIPTION - Preparation of livestock and poultry manure biological organic fertilizer comprises:    (A) preparing chicken manure and additive, selecting one block flat ground flat with no water pool, seperating chicken manure and additive, dividing 1000 kg chicken manure into five parts;    (B) selecting building fermentation platform;    (C) mixing compost mixture with strain, stirring uniformly, adjusting chicken manure water content to 60%, processing other four stacks of chicken manure;    (D) fermenting compost, after first fermentation stage, automatically raising temperature to more than 55 degrees C, keeping for 5-7 days, turning once after 3 days, fermenting for 7-10 days, naturally reducing temperature to less than 50 degrees C, adding 5-8 kg bacteria mixture, stirring uniformly, controlling water content at 50%; performing second fermentation at less than 50 degrees for 10-20 days, reducing compost temperature to less than 40 degrees C; and    (E) drying fermented finished product, crushing, sieving, and packaging.    The strain comprises 0.2% Azotobacter, 0.3% potassium solubilizing bacteria, 0.3% phosphorus solubilizing bacteria, 0.5% yeast and 0.2% Bacillus subtilis.
NOVELTY - Fermentation of mushroom compost waste comprises stacking waste mushroom slag; preparing additive solution comprising fermentation microorganism, urea and dry sesame slag; spraying uniformly additive solution on mushroom residue; performing heat and moisture insulation processing, maintaining fermentation at 50-60 degrees C; and testing if electrical conductivity is more than 2.5.    USE - Method for fermenting mushroom compost waste used for preparing plant culture medium (claimed).    DETAILED DESCRIPTION - Fermentation of mushroom compost waste comprises:    (A) stacking waste mushroom slag to 0.3-2.0 m;    (B) per cubic meter of waste mushroom residue, weighing additive comprising 0.05-0.5 kg fermentation microorganism, 0.1-1.5 kg urea and 0-5 kg dry sesame slag, adding in water, stirring uniformly to obtain additive solution;    (C) spraying uniformly additive solution on mushroom residue to obtain water content of 55-60%;    (D) performing heat and moisture insulation processing, maintaining fermentation at 50-60 degrees C;    (E) when mushroom residue substrate core temperature is not lower than 65 degrees C, turning once; and    (F) when mushroom residue matrix core temperature is more than 50 degrees C for more than three months, testing if electrical conductivity is more than 2.5.    An INDEPENDENT CLAIM is included for preparation of plant culture medium comprising carrying out fermentation of mushroom compost waste; mixing fermented material with vermiculite at volume ratio of 6:4, mixing and stirring uniformly; and washing with clean water mushroom residue.
NOVELTY - Automatic microbial reactor comprises material storage device (1), blending machine (2), screw feeding device (3), barrel, feed port, second helical sheet, second rotation lever, second driving unit (4), screw feeding device (5), first helical sheet, first rotation lever, extension, first driving unit (6), exhaust system (7), exhaust fan, line, storage tank, pump, aqueduct, return pipe, powder dosing device (9), silo, first weighing device, second weighing device (10), sleeve (11), discharge port, operating platform (12) and staircase (13).    USE - Automatic microbial reactor used for recycling waste materials.    ADVANTAGE - The device is energy-saving and cost-saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of automatic microbial reactor.    Material storage device (1)    Blending machine (2)    Screw feeding device (3)    Second driving unit (4)    Screw feeding device (5)    First driving unit (6)    Exhaust system (7)    Powder dosing device (9)    Second weighing device (10)    Sleeve (11)    Operating platform (12)    Staircase (13)
NOVELTY - A coastal saline-phosphogypsum fertilizer applying method involves applying phosphogypsum to coastal saline soil in rice field, and applying special fertilizer comprising organic and inorganic compound fertilizer with organic matter of 15-30 wt% to saline alkali soil planting rice field.    USE - Method for applying coastal saline-phosphogypsum fertilizer.    ADVANTAGE - The method enables applying coastal saline-phosphogypsum fertilizer with improved agricultural production level and production efficiency.
NOVELTY - Synthesizing symmetrical diaryl disulfide (I) comprises reacting elemental sulfur and aryl boronic acid (II) using solvent and copper salt catalyst at 50-80 degrees C for 5-8 hours.    USE - The method is useful for synthesizing (I) (claimed).    ADVANTAGE - The method is safe, less-toxic, simple, environmentally friendly and utilize less dosage of catalyst.    DETAILED DESCRIPTION - Synthesizing symmetrical diaryl disulfide of formula (I) comprises reacting elemental sulfur and aryl boronic acid of formula (II) using solvent and copper salt catalyst at 50-80 degrees C for 5-8 hours.    R = H, 2-CH3, 3-CH3, 4-CH3, 2-OCH3, 3-OCH3, 4-OCH3, 4-Cl, 4-Br, 4-CN, 4-F, 4-CF3, 4-NO2 or 1-naphthyl.
NOVELTY - Use of biological enzyme liquid is claimed for decomposing humic acid, improving content of free radicals, ion exchange and complexing ability, and complexation reactions.    USE - The biological enzyme liquid is useful for decomposing humic acid, improving content of free radicals, ion exchange and complexing ability, and complexation reactions. The biological liquid is also useful as plant fertilizer and improving biological activity in soil, controlling weed (claimed), and promoting plant growth.    ADVANTAGE - The method improves utilization of urea and prevents pollution.
NOVELTY - Use of fertilizer composition is claimed for cultivating rice in water culture without soil.    USE - The fertilizer composition is useful for cultivating rice in water culture without soil (claimed).    ADVANTAGE - The fertilizer composition is applied to the existing rice cultivation to produce rice raw material or finished product, preferably pitavastatin based on requirement of silicon and calcium nutrients and to raise the silicon and calcium nutrients in suitable proportion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the composition, which involves obtaining 50% manure, 10% ash, 20% calcium silicate fertilizers, 10% phosphate fertilizer and 10% magnesium fertilizer, mixing the raw materials, fermenting the mixture for 10-30 days, mixing same amount of calcium silicate fertilizer, phosphate fertilizer and magnesium fertilizer and adding 10% potassium fertilizer, fermenting the mixture 10 days to obtain the product.
NOVELTY - Manufacturing Tylenol (RTM: N-acetyl-p-aminophenol), comprises performing microwave heating reaction on 4-aminophenol and acetic acid, promoting dehydrocondensation reaction, and rapidly evaporating by-product water to obtain the product.    USE - The method is useful for manufacturing Tylenol (RTM: N-acetyl-p-aminophenol) (claimed).    ADVANTAGE - The method utilizes microwave by eliminating the use of acid catalysts, which causes adverse effects on the environment, suppresses the generation of acetic acid by-product, improves economical efficiency by improving fast reaction speed (claimed), has high yield rate of 92%, shortens the reaction time from 2 hours to 4 minutes, is performed under solvent-free environmentally friendly condition, utilizes beaker containing alumina to prevent overheating and sequential microwave irradiation method instead of continuous microwave irradiation method, and satisfies the crisis of Korea-US FTA by producing modified drugs in national developing markets.
NOVELTY - Preparation of phytic acid involves mixing an alginic acid solution and an aqueous solution comprising calcium and iron, loading the obtained mixture to affinity chromatography column beads, injecting rice bran powder in 0.01N hydrochloric acid solution, reacting at 90-110 degrees C for 3-9 hours, refluxing, and then purifying by chromatographic analysis.    USE - Preparation of phytic acid used for functional cosmetic.    ADVANTAGE - The method efficiently and economically provides phytic acid of high purity without causing pollution to environment.
NOVELTY - A quick-release fexofenadine pellet comprises 50-35.0 g pseudoephedrine slow-release pellet and 100 mL fexofenadine suspension liquid coated on surface of pellet.    USE - Quick-release fexofenadine pellet used in field of medicine.    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production. The medicine has fast and stable effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of quick-release fexofenadine pellet comprising weighing and stirring water and disintegrating agent, adding adhesive, uniformly stirring, slowly adding fexofenadine and release agent, stirring until suspension is viscous to obtain suspension liquid, taking pseudoephedrine slow-release pellet, adding into coating machine, adjusting fan frequency to 22.00-45.00 Hz, air inlet temperature to 40.0-60 degrees C, material temperature to 35.0-58.0 degrees C, speed to 80-150 revolutions/minute and atomizing pressure to 2.00-3.20 bar, spraying suspension liquid, drying and sieving.
NOVELTY - 2-Pyrimidin-2-yl-benzonitrile compounds (I) are new.    USE - Used as 2-pyrimidin-2-yl-benzonitrile compounds.    ADVANTAGE - The method: utilizes easily available raw materials and moderate reaction conditions; is simple; produces the product with maximum yield of 90%; is environmentally friendly; and is suitable for industrial production.    DETAILED DESCRIPTION - 2-Pyrimidin-2-yl-benzonitrile compounds of formula (I) are new.    R1 = -CH3, -OCH3, -Cl or toluenesulfonyl; and    R2 = -H, -C2H5 or phenyl.    An INDEPENDENT CLAIM is also included for the preparation of (I).
NOVELTY - Fertilizer composition comprises yogurt, dry yeast, sugar, soybean and water that are mixed and fermented at a temperature of 35-45 degrees C for 20-50 hours to obtain 1-20 wt.% of a fermented product, and 80-99 wt.% of water.    USE - The fertilizer composition is useful for improving the plant growth and protecting root and stem of the plant.    ADVANTAGE - The fertilizer composition is eco-friendly.
NOVELTY - The present invention is growing of four Plant growth promoting Rhizobacterial consortium in a single base medium. Treating this medium with different cell protectant chemicals to improve survival and stability of these bacterial consortium for long period in the pack. Improved survival on the seeds after coating. His preparation includes the growing of bacterial consortium upto the stationery pahse. The method includes addition of cell protectants to the growing medium at the end of exponential phase to alter the liquid properties. The liquid microbial inoculants with specified bacterial strains can be stored Ifor longer periods . The LIQUID inoculants can be either applied on the seed or directly can be applied to he field soil at the time of sowing along with organic manure.
NOVELTY - Preparation of abacavir (II) or its salt, comprises: (a) reacting N-(2-amino-4,6-dichloro-5-pyrimidinyl) formamide (III) with (1S,4R)-(4-aminocyclopent-2-enyl)methanol (IV) or its salt, in presence of base to give (1S,4R)-4-((2-amino-6-chloro-5-formamido-4-pyrimidinyl)amino)-2-cyclopentene-1-methanol (V); (b) cyclizing (V) with a cyclizing reagent to provide (1S,4R)-4-((2-amino-6-chloro-9H-purin-9-yl))-2-cyclopentene-1-methanol (VI) or its salt; (c) reacting (VI) with cyclopropylamine to provide abacavir (II); and (d) optionally, converting abacavir into its salt.    USE - The processes are useful for preparation of abacavir or its salt, and an amorphous form of abacavir (all claimed), where the abacavir is useful for treating HIV-1 infection. No biological data given.    ADVANTAGE - The process provides abacavir or its salt in a cost effective and environmental friendly manner.    DETAILED DESCRIPTION - Preparation of abacavir of formula (II) or its salt, comprises: (a) reacting N-(2-amino-4,6-dichloro-5-pyrimidinyl) formamide of formula (III) with (1S,4R)-(4-aminocyclopent-2-enyl)methanol of formula (IV) or its salt in presence of base to give (1S,4R)-4-((2-amino-6-chloro-5-formamido-4-pyrimidinyl)amino)-2-cyclopentene-1-methanol of formula (V); (b) cyclizing (V) with a cyclizing reagent to provide (1S,4R)-4-((2-amino-6-chloro-9H-purin-9-yl))-2-cyclopentene-1-methanol of formula (VI) or its salt; (c) reacting (VI) with cyclopropylamine to provide abacavir (II); and (d) optionally, converting abacavir into its salt. An INDEPENDENT CLAIM is also included for preparing an amorphous form of abacavir, comprising: providing a solution of abacavir in a solvent or mixture of solvents; and isolating the amorphous form of abacavir.
NOVELTY - This utility model claims a kind of urban and rural solid waste innoxiously processing comprehensive utilization system, comprising a weighing and metering device, sorting device, high-temperature anaerobic fermentation device of organic matter, plastic granulating device, pyrolysis and gasification device of construction waste crushing device, a building material manufacturing device and dust removing and odour removing device. A " comprehensive processing method for domestic garbage, medium temperature anaerobic fermentation, plastic pelleting system, gasification system, a building material manufacturing system wherein each component are combined with the comprehensive processing method, the industry garden garbage as the material out of a, it basically realizes zero filling, ensures garbage, and the process, which effectively reduces the secondary pollution, reduce urban environment pollution caused by the waste.
NOVELTY - This utility model belongs to marsh gas engineering and environmental engineering field, claims a feed device of anaerobic reactor, wherein the feeding device comprises an upper end of the eccentric different-diameter pipe and straight pipe of the lower end of the eccentric different-diameter pipe and the straight pipe is an integral structure, the straight pipe extends into the anaerobic reactor via anaerobic reactor top cover. This utility model claims a anaerobic reactor feed device, solving the problem that the feeding hole is easy to be blocked and batch feeding effect, further, this utility model claims a anaerobic reactor feeding device, a clamp is connected with the anaerobic reactor top cover, good leak tightness, simple assembling mode, which is convenient to dismount.
NOVELTY - A kind of kitchen garbage anaerobic digestion treatment device, comprising a reactor tank body, the tank body is provided with a storage bag, air bag and the amount indication meter is connected with the top of the reactor tank body is further provided with an exhaust port and a feeding port, the outer wall of the reactor tank body is connected with a heating heat preservation layer, the inner wall of the reactor tank body is set with safe anti-explosion layer, one side of the reactor tank body is set in a stirrer, a reactor tank body is provided with a circulating pump, the bottom of the reactor tank body is provided with a discharging port, the upper part of the material outlet is set in the sand emptying device, a reactor tank body is provided with a temperature sensor and the pressure sensor, quantity indicator, heating heat preservation layer, a stirrer, a circulating pump, a temperature sensor and a pressure sensor are connected with the control cabinet, a stirrer for stirring the materials, the temperature sensor transmits the material temperature to the control cabinet, heating heat preservation layer, a pressure sensor for detecting the pressure reactor tank body, air volume is small, which saves cost and high safety and reliability characteristics of a discharge port,.
NOVELTY - A crop straw pre-processing reaction tank comprises tank jacket (1), and tank body (2) provided with upper sealing head (3) at top which is composed of feed inlet port (5), material sampling port (6), and outlet port (7), lower sealing head (4) at bottom, oxygen pipe (8), stirring and conveying device, and discharging pipe (9) at lower end.    USE - A crop straw pre-processing reaction tank (claimed).    ADVANTAGE - Crop straw pre-processing reaction tank is environment-friendly, low in cost, and capable of aerobic, micro-aerobic, and anaerobic biological pretreatment of crop straw, and has convenient operation, high processing efficiency, and low power consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic diagram of a crop straw pre- processing reaction tank.    Tank jacket (1)    Tank body (2)    Upper sealing head (3)    Lower sealing head (4)    Feed inlet port (5)    Material sampling port (6)    Outlet port (7)    Oxygen pipe (8)    Discharging pipe (9)
NOVELTY - The utility model relates to the automatic watering plant decentralized treatment of domestic waste water device. A connecting pipe, a water collecting sedimentation, a water distributing pipe, a plant ecological treatment tank. A connecting pipe, water level drain pipe is connected with the waste outlet main pipeline and main pipeline connected with water level, a water collecting sedimentation of sewage collecting pipe provided with a filter screen, a water collecting settling pipe and water distribution pipe by the siphon pipe is connected with the siphon pipe with the water distributing pipe through valve, plant ecological processing tank divided pass through overflow groove baffle is processing area and an overflow groove, a water distribution pipe on the plant ecological treatment tank by the baffle plate, and a gravel, or small pebbles. This utility model can automatically collect waste water pipeline, a siphon principle through the plant automatic irrigating in the box body, the plant irrigating by use amount of water, reduces discharging sewage pollutant concentration. The utility model can be widely applied to the scattered domestic sewage treatment of town, community resident building, villa and vacation village, and so on, and wide application range.
NOVELTY - This utility model claims a mixed filler of the artificial wetland purification experiment device, wherein it is composed of a water distribution layer, soil layer, filler layer, a gravel layer, a granite layer, a drain valve and a barrel, wherein the water distribution layer, soil layer, filling layer, fine stone layer and the granite layer is set on the barrel, arranged in order from top to bottom, wherein the drain valve is set on the 3-4 cm of the barrel wall. The height of said fine sand filling layer is 14 cm, the fine sand filling layer is nano-grade silicon dioxide and silver sand.... according to the ratio of 1: 16. This utility model is capable of providing the basis carbon source and nitrogen source and nutrient substance for the growth and propagation of microorganism and aquatic plant to supply stable attached surface of the filtrating device used to filtrate sewage suspended substance, removing nitrogen and phosphorus and so on through physical and chemical function.
NOVELTY - This utility model claims a load suspending filler in circulating fluidized bed waste water treatment device, comprising a manifold in fluid communication with the water pump connected with the fluidized bed reaction pool, in the fluidized bed reaction tank are respectively provided with a transmission hole aeration system, suspending the PVA filler and anti-loss network, the fluidized bed reaction pool and the deposition return-flow system are connected with each other. The device uses biological method processing method, making the pollutant and waste water in the biochemical function, removing in the fluidized bed reaction tank and degrade pollutant in the waste water, the purified water. The device can use the traditional active sludge method and biological film method waste water processing technology, it has the advantages of, improves the concentration of common sludge, reduces the waste water processing system floor area and investment, increases in the sewage CODcr, BOD5, the total nitrogen and the ammonia nitrogen removing efficiency and so on.
NOVELTY - The utility model claims an overflow double-cyclic anaerobic reactor, comprising a reactor main body, a circulating stirring device, the top of the main body reactor of sludge discharging device and discharging device, the top of the main body is provided with a feeding pipe and a marsh gas pipe, a circulating stirring device comprises a circulating stirring device and is used for pushing the fermentation liquid in the circulating stirring device of a circulating flow in the reactor main body, a sludge discharging device comprises an overflow groove, the lower end is extended into the overflow pipe of the overflow groove to the bottom of the reactor main body and the upper end of the overflow groove on the outer wall of the pipe, the discharging pipe discharging device comprising a gate, scum groove and a floating slag groove wall. This utility model increases the turbulence degree of the mass transfer effect is high, removing the short circuit and dead area, avoid the sediment, reduces the slag foam area, a rate is low, volume production rate and reactor efficiency, ensure that there is no negative pressure is generated in the reactor through the overflow discharge mode, the feeding pipe and the circulating pipe, the fermentation raw material in advance.
NOVELTY - Preparing animal derived amino acid organic farming materials using recycled butchery blood, by collecting animal blood produced in slaughterhouse, grinding collected blood, adding decomposing enzymes to processed blood, cooling blood to room temperature, and adding preservative to the blood for preventing contamination of the blood, and deodorizing agent to the blood.    USE - The method is useful for preparing animal derived amino acid organic farming materials using recycled butchery blood (claimed).    DETAILED DESCRIPTION - Method for preparing animal derived amino acid organic farming materials using recycled butchery blood, involves (a) collecting animal blood produced in slaughterhouse, inside a container, (b) subjecting collected blood to fine grinding process to obtain particle size of 0.4-0.9 mesh, (c) adding decomposing enzymes to processed blood and maintaining the blood at 36-75 degrees C such that enzyme decomposition of blood takes place, (d) cooling the blood to room temperature, and (e) adding preservative to the blood for preventing contamination of the blood, and deodorizing agent to the blood, where preservative is added in an amount of 3-10 pts. wt. with respect to 100 pts. wt. blood. An INDEPENDENT CLAIM is included for animal derived amino acid organic farming materials prepared by the above-mentioned method.
NOVELTY - Hybrid thermophilic anaerobic digestion process for combined treatment of food waste and livestock manure, involves (a) crushing food waste, performing anaerobic hydrolysis of crushed product and introducing product into high temperature digester, (b) adding livestock manure to the product, maintaining pH and temperature, and adding obtained mixture into mesophilic digester, (c) maintaining the mixture, filtering solids by filter, and recycling the filtrate, and (d) supplying combined heat generated biogas generator (CHP) to the product, and processing waste product.    USE - The process is useful for hybrid thermophilic anaerobic digestion for combined treatment of food waste and pig manure (claimed).    DETAILED DESCRIPTION - Hybrid thermophilic anaerobic digestion process for combined treatment of food-waste and pig-manure, involves (a) crushing food waste in closed crude acid degradation, performing anaerobic hydrolysis of crushed product at 10-50 degrees C for 1-10 days and introducing obtained product into high temperature digester, (b) adding livestock manure to the product, maintaining pH of the mixture to 6-8 and temperature digestion at 50-80 degrees C for 5-20 days after high-temperature anaerobic methane fermentation, and adding obtained mixture into mesophilic digester, (c) maintaining the mixture in mesophilic digester at 20-40 degrees C for 1-10 days after stabilization, filtering anaerobic digestion solids by filter, and recycling the filtrate, and (d) supplying combined heat generated biogas generator (CHP) to the product, and processing waste product.
NOVELTY - Invention relates to agriculture. The method producing organic fertiliser involves fermentation of a raw product, removing biogas, separation, wherein the raw product used is in form of bird or animal excrement which undergoes preliminary fermentation; after fermentation and removal of biogas, the dense component of the raw product is separated from the fermentation product and the liquid component is mixed with a flocculant; the flocculation product is settled until achieving separation of the solid fraction and the liquid fraction in a ratio from 1:3 to 1:5; the liquid fraction is removed and the remaining product is decanted to moisture content of 40-50%; the liquid component is removed and the decanted mass is mixed with the dense component of the separation product and pressed with an auger device or is first pressed with an auger device and then mixed with the dense component of the separation product that has been pressed with an auger device, wherein at the outlet of the auger device, the product has moisture content of 20-30%, after which the product is heat dried at temperature of 40-60 degrees C to moisture content of 10-15%.    USE - Chemistry.    ADVANTAGE - Invention reduces power consumption when generating heat energy for thickening a product of fermenting bird and animal excrement, enables to preserve organic and mineral substances in the end product, improves environmental friendliness of the method.5 cl, 2 tbl
NOVELTY - The device has generating device (1) that is installed on supporting device (2). A tile (3) is connected to main portion for methane production through the supporting device. The methane producing device is provided with material conveying and discharging device, storage unit and a marsh gas generating device. A supporting device is provided for performing solid-liquid separation of the slag.    USE - Marsh gas producing device.    ADVANTAGE - The feeding of raw material can be effectively controlled so that the production efficiency of the marsh gas producing device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the marsh gas producing device.    Generating device (1)    Supporting device (2)    Tile (3)
NOVELTY - A lipase producing bacterium Pseudomonas mendocina PMMA (CGMCC NO: 7644), is new.    USE - The bacteria P.mendocina PMMA is useful for producing lipase used in preparation of biodiesel (claimed).    ADVANTAGE - The method is simple and cost-effective, and has improved transfer rate and conversion rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of producing magnetic chitosan microsphere, involves selecting magnetic powder of less than 100 nm, 1-2 pts. wt. ferric oxide, 0.5-1.5 pts. wt. chitosan and 2-4 pts. wt. oil, 20-25 pts. wt. 1% hydrochloric acid aqueous solution, 20% sodium hydroxide aqueous solution and 30% formaldehyde aqueous solution, mixing the raw materials, subjecting the mixture to solvent ultrasonic treatment, uniformly mixing, gradually adding condensed liquid and stirring by magnetic force to obtain polymeric microsphere of 2-5 mm; and    (2) method of producing biodiesel using lipase producing bacteria, involves adding lipase producing bacteria into phosphate buffer solution, shaking uniformly, preparing cell suspension, reacting the cell suspension and magnetic chitosan microsphere at 30-40 degrees C for 18-24 hours, processing the mixture at 120-150 rotations/minute with permanent magnet, using phosphate buffer solution repeatedly washing and obtaining the magnetic immobilized cell catalyst.
NOVELTY - Enzymolyzing and saccharifying biomass, involves soaking lignocellulosic biomass in peroxide solution, filtering and separating the mixture to obtain hydrolyzed solution A and wet residue A, washing waste liquid using acid, filtering the separated wet residue A, adding acid washed waste liquid, processing the mixture and performing solid-liquid separation to obtain hydrolyzed solution B and wet residue B, and washing the wet residue B at normal temperature using deionized water to obtain the product.    USE - The method is useful for enzymolyzing and saccharifying biomass to produce soluble-sugars (claimed).    ADVANTAGE - The method reduces dosage of cellulase and enzymolysis time and thus is cost-effective, produces soluble-sugar in high yield, and improves conversion rate of biomass.    DETAILED DESCRIPTION - Method for enzymolyzing and saccharifying biomass, involves soaking lignocellulosic biomass in 0-6% peroxide solution for 10-300 minutes at 20-80 degrees C, filtering and separating the mixture to obtain hydrolyzed solution A and wet residue A, washing waste liquid using acid, filtering the separated wet residue A at 80-150 degrees C, adding 3-10 times of acid washed waste liquid, processing the mixture for 2-120 minutes and performing solid-liquid separation to obtain hydrolyzed solution B and wet residue B, and washing the wet residue B at normal temperature using deionized water for 3 times to obtain the product.
NOVELTY - Method for preparing soil nutritional disinfectant involves selecting water retaining agent, dissolving 30 kg urea, 5 kg potassium dihydrogen phosphate and 2 kg carbendazim in 1000 kg water, obtaining nutritional disinfectant, mixing 1000 kg nutrition disinfectant and 4-5 kg water retaining agent, processing for 20-30 minutes, obtaining solid nutrition disinfectant, mixing soil and solid nutrition disinfectant, stirring, forming cultivation bed, un-bagging and spreading tricholoma lobayense sticks, covering with the special soil covering material, maintaining and fruiting.    USE - Method for preparing soil nutritional disinfectant used for cultivating tricholoma lobayense.    ADVANTAGE - The method efficiently provides soil covering material having excellent nutrition and moisture-retaining effect for prolonged period of time and enables cultivation of tricholoma lobayense with high yield and stability.    DETAILED DESCRIPTION - Method for preparing soil nutritional disinfectant involves dissolving 30 kg urea, 5 kg potassium dihydrogen phosphate and 2 kg carbendazim in 1000 kg water, obtaining nutritional disinfectant, mixing 1000 kg nutrition disinfectant and 4-5 kg water retaining agent, processing for 20-30 minutes, obtaining solid nutrition disinfectant, mixing 1000 kg soil and 600 kg solid nutrition disinfectant, stirring, forming cultivation bed with width of 100-120 cm and depth of 20-25 cm, un-bagging and spreading tricholoma lobayense sticks, covering with the special soil covering material, maintaining and fruiting.
NOVELTY - Method for planting fast-growing plant by comprehensive utilization of alternative device to replace fossil energy, involves planting and/or cultivating fast-growing herbaceous and woody plant, algae or bryophytes in selected area of land or water, growing the plant over a period of time for harvesting or collecting the plant with proper height or size, naturally drying the harvested or collected plants, processing the dried plant to section, performing compression molding process, storing and sealing the plants, and processing the plant to obtain e.g. solid fuel.    USE - The method is useful for planting fast-growing plant by comprehensive utilization of alternative device to replace fossil energy (claimed).    ADVANTAGE - The method provides product with high purity, and is suitable for industrial production.    DETAILED DESCRIPTION - Method for planting fast-growing plant by comprehensive utilization of alternative device to replace fossil energy, involves (a) planting and/or cultivating fast-growing herbaceous and woody plant, algae or bryophytes in selected area of land or water, (b) growing the plant over a period of time for harvesting or collecting the plant with proper height or size, (c) naturally drying the harvested or collected plants, (d) processing the dried plant to section, and performing compression molding process, (e) storing and sealing the molded plants, and (f) processing the plant to obtain solid fuel, liquid fuel, gas fuel or directly supply of electricity and power, and replacing fossil energy.
NOVELTY - Method for preparing maggot peptide, involves (a) inoculating microorganism capable of producing protease in sterile culture medium, and culturing the microorganism to obtain microbial spores, (b) inoculating microbial spores to a culture medium provided with only nitrogen source, performing fermentation for 12-100 hours to obtain maggot protein, and removing the mycelial pellets or biomass to obtain maggot peptide solution, and (c) drying the maggot peptide solution at low temperature to obtain product.    USE - The method is useful for preparing maggot peptide (claimed).    ADVANTAGE - The method is simple to perform and cost-effective, and provides high yield of maggot peptide.
NOVELTY - Citrulline is purified by peeling watermelon, crushing, removing seeds, cleaning stem, crushing, mixing, treating with pectinase, and filtering; vacuum concentrating, refrigerating, collecting, separating, and purifying; passing through anion exchange resin, eluting with ammonia water, collecting eluent, decoloring eluent by activated carbon adsorption, and filtering; decompressing, distilling, concentrating, and crystallizing; and washing with deionized water and ethanol, recrystallizing, collecting citrulline, and adjusting pH value of liquor to obtain glutamic acid.    USE - Method for purifying citrulline (claimed).    ADVANTAGE - The process has 3% yield, high purity, and low energy consumption.    DETAILED DESCRIPTION - Citrulline is purified by:    (A) peeling watermelon, crushing, removing seeds, cleaning stem, crushing, mixing, treating with pectinase for 30-60 minutes, and filtering; vacuum concentrating, adjusting pH value to 10.76, refrigerating at 1 degrees C overnight, collecting crystals, separating, and purifying;    (B) passing through anion exchange resin at 20-25 degrees C, washing with deionized water, eluting with ammonia water, collecting eluent, decoloring eluent by activated carbon adsorption for 40-60 minutes, and filtering;    (C) decompressing, distilling, concentrating, and crystallizing at 40-50 degrees C; and    (D) washing with deionized water and ethanol, recrystallizing for 2-3 times, collecting citrulline, and adjusting pH value of liquor to 3.22.
NOVELTY - The system (1) has liquefaction unit (100) that liquidizes the supplied natural gas to the ultralow temperature. A reboiler (400) supplies the heat to the lower unit of column (200) and heats the light nitrogen component. A reflux unit (300) exchanges the heat in the column according to the removed methane liquid while supplying the natural gas liquefied in the liquefaction unit. The liquefaction unit separates the nitrogen gas condensed from the methane liquid.    USE - Nitrogen rejection system for natural gas.    ADVANTAGE - The refrigeration load of the refrigeration cycle can be reduced by supplying the nitrogen to the column after exchanging heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for nitrogen rejection method for natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the nitrogen rejection system for natural gas.(Drawing includes non-English language text)    Nitrogen rejection system for natural gas (1)    Liquefaction unit (100)    Column (200)    Reflux unit (300)    Reboiler (400)
NOVELTY - Producing a UV-resistant gelatin/silica coated viral particle comprises: mixing a gelatin solution with a viral solution to form a mixture; adding a silica solution into the mixture to form a precipitate, where the silica solution has a pH value of 5; and immersing the precipitate into a green tea extract for at least 30 minutes so that the green tea extract is absorbed by the precipitate and for forming the gelatin/silica coated viral particle.    USE - The method is useful for producing a UV-resistant gelatin/silica coated viral particle, which is useful for controlling agricultural pests in an agricultural field (all claimed), where the pest includes insects. Test details are described but no results given.    ADVANTAGE - The method safely and conveniently produces the UV-resistant gelatin/silica coated viral particle with improved shelf life stability in an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a UV-resistant gelatin/silica coated viral particle produced by the method having a Baculovirus, and a gelatin/silica coating disposed outside the Baculovirus, where the gelatin/silica coating has a porosity of 1-10 nm, and further includes a green-tea extract, which is absorbed in the porous structure of the gelatin/silica coating.
NOVELTY - Making negative carbon fuel from a carbon-containing input (200), comprises: subjecting a carbon-containing input to a thermal process to obtain a volatile gas stream and an inert carbonaceous solid, where the volatile gas stream and the inert carbonaceous solid are formed as separate components in the process, and a portion of the carbon from the carbon-containing input is contained in the inert carbonaceous solid; and converting the volatile gas stream to one or more of combustible fuels (290), refinery feedstock or chemicals.    USE - The method is useful for making negative carbon fuel (claimed) for combustion in an automobile or aviation engine.    ADVANTAGE - The method provides separate and uncontaminated negative carbon fuel products in a simple manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a method of for making negative carbon fuel.    Carbon-containing input (200)    Sequesterable carbon (270)    Combustible fuels. (290)
NOVELTY - Method of preparing nano-pesticide involves performing emulsion - solvent evaporation of poly (lactic-co-glycolic acid) and thiophanate-methyl to obtain product.    USE - The method is useful for preparing nano-pesticide for controlling plant pathogenic fungi (claimed).    ADVANTAGE - The method is economic and enables to prepare nano-pesticide which is effective at low dosage, nontoxic to humans and animals and environmentally-friendly, does not form residues, delays the generation of pest resistance and has broad insecticidal spectrum.
NOVELTY - Herbicidal composition comprises flumiclorac-pentyl and traloxydim.    USE - The herbicidal composition in the form of wettable powder or water dispersible granule is useful for controlling wheat field weeds (all claimed), broadleaf weeds and grassy weeds.    ADVANTAGE - The herbicidal composition is synergistic, effective at reduced dosage for long period of time and environmentally-friendly, delays the generation of weed resistance and has expanded herbicidal spectrum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition which involves mixing the above-mentioned raw materials with auxiliary material.
NOVELTY - A florfenicol colistin sulfate powder contains 5-20 wt.% florfenicol, 2-20 wt.% colistin sulfate, 0.5-2 wt.% borax, 5-30 wt.% citric acid, 0.1-2 wt.% potassium bicarbonate, 7.5-30 wt.% polyvinylpyrrolidone, 1-5 wt.% poloxamer 188, and balance anhydrous glucose.    USE - A florfenicol colistin sulfate powder (claimed).    ADVANTAGE - Powder is soluble and has better synergistic antibacterial effect and preparation process is simple, convenient, and environment-friendly and has improved production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of florfenicol colistin sulfate powder which involves dissolving polyvinylpyrrolidone in absolute ethyl alcohol, addnig florfenicol, citric acid, borax, potassium bicarbonate, and poloxamer 188, uniformly mixing components to obtain soft material, recovering absolute ethyl alcohol by drying to obtain solid component, crushing solid component to obtain powder, adding colistin sulfate and anhydrous glucose, and unifromly mixing components.
NOVELTY - A copper-based carbon dioxide methanation catalyst comprises copper-based metal (M) oxide as main active component, in which is metal (M) comprises copper, cobalt, aluminum, zinc, magnesium, and iron or manganese.    USE - Copper-based catalyst is used in carbon dioxide methanation reaction (claimed) for producing natural gas rich in carbon dioxide and hydrogen, and carbon dioxide emission field.    ADVANTAGE - The copper-based carbon dioxide methanation catalyst has high activity and methane selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of copper-based carbon dioxide methanation catalyst, which involves mixing salt solution of metal (M) and alkaline solution, co-precipitating the mixture using hot de-mineralized water, filtering, drying the filter cake, and calcining the dried filter cake; and    (2) evaluation method of activity of copper-based carbon dioxide methanation catalyst, which involves placing the catalyst in a intermediate temperature zone of a fixed bed reactor with quartz sand support, carrying out carbon dioxide methanation reaction at 290-450 degrees C under pressure of 4-6 Mpa with space velocity of 5000-12000 hour-1 and hydrogen and carbon dioxide ratio of 3.1-4.1, and analyzing the obtained reaction product by gas chromatography.
NOVELTY - A layered double hydroxide hybrid material comprises bivalent metal salt and bovine serum albumin-aluminum sol. The bivalent metal is magnesium, nickel, manganese and/or zinc. The molar ratio of bivalent metal salt to aluminum is 1:3-3:1. The hybrid material is obtained by in-situ growth reaction.    USE - Layered double hydroxide hybrid material for use in biological applications.    ADVANTAGE - The layered double hydroxide hybrid material has nano hierarchical structure, excellent biological compatibility, controlled shape, and is manufactured with high yield, by simple and environmentally-friendly process without requiring special equipment and reaction condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the layered double hydroxide hybrid material, which involves stirring 0.01% aluminum salt aqueous solution and 0.1-10 g/l bovine serum albumin at 8-10 degrees C for 5 hours to obtain solution (A), adding aqueous ammonia to the obtained sol to adjust pH to neutral, producing milky white material, preparing precipitating agent solution containing bivalent metal salt aqueous solution and precipitating agent, adding the sol to precipitating solution, reacting the contents at 40-95 degrees C, filtering using water and ethanol, and drying the filtered material at 50-90 degrees C for 12-24 hours to obtain the hybrid material.
NOVELTY - The reactor has greenhouse (19) whose top section is provided with glass roof (8) set with solar system (10) and middle section is provided with screen. Earthworm compost processing area (3) is set at lower end of discharging system (4). Thermometer (13) inserted in greenhouse, temperature and humidity on-line analysis system (14), oxygen concentration analysis system (15) and air conditioner (16) are connected with gas concentration on-line analyzing system (17) respectively. Data processing system (18) is connected to gas concentration on-line analyzing system.    USE - Full-automatic greenhouse earthworm reactor.    ADVANTAGE - The generation of pollution can be avoided, since earthworm biological organic garbage processing process is performed. The constant temperature can be maintained in the reactor by performing temperature online monitoring process. By utilizing the solar heat, energy can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the full-automatic greenhouse earthworm reactor.    Earthworm compost processing area (3)    Discharging system (4)    Glass roof (8)    Solar system (10)    Thermometer (13)    Temperature and humidity on-line analysis system (14)    Oxygen concentration analysis system (15)    Air conditioner (16)    Gas concentration on-line analyzing system (17)    Data processing system (18)    Greenhouse (19)
NOVELTY - Bio-organic fertilizer is prepared using 15-24 pts. wt. microbial inoculum, 20-26 pts. wt. straw, 7-12 pts. wt. wheat bran, 6-10 pts. wt. cultivated mushroom residue, 2-6 pts. wt. sawdust, 1-3 pts. wt. corn powder, 1-3 pts. wt. golden cypress and 10-19 pts. wt. water, where 1% microbial inoculum is obtained by mixing EM (RTM: Effective microorganisms), yeast and nitrogen-fixing bacteria in ratio of 3:1:1.    USE - As bio-organic fertilizer for soybean (claimed).    ADVANTAGE - The bio-organic fertilizer is cost-effective and prepared by easy method and makes use of waste material and hence environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the bio-organic fertilizer which involves (a) weighing the above-mentioned raw materials and preparing microbial inoculum; (b) mixing straw, wheat bran, cultivated mushroom residue, sawdust, corn powder and golden cypress to obtain mixture; (c) adding water to the microbial inoculum prepared in step (a) to obtain inoculum spray liquid; (d) transferring the mixture obtained in step (b) to fermentation tank, adding 1/5 weighed rice straw, 1/5 inoculum spray liquid obtained in step (c) and 1/5 weighed soybean straw and simultaneously adding remaining raw materials into the fermentation mixture and fermenting for 7-20 days to obtain fermented wet material; and (e) drying the obtained fermented wet material 30-50 degrees C to have 10 wt.% moisture content, grinding dried material, packaging and storing product.
NOVELTY - The device has a fermentation chamber that is made of PVC and a fermentation cabin that is installed on stainless steel bracket (21). A guide folded plate (9) is provided with a hole cover plate (12). A ventilation system is provided with an air pump (16), a flow meter (14), and electromagnetic valve (15). The flow meter and electromagnetic valve are set close to air pump. A real-time online monitoring device is provided with an oxygen monitor (18), a temperature monitor (19), a carbon dioxide monitoring circuit (22), and ammonia and sulfureted hydrogen monitoring circuit (24).    USE - Cabin type aerobic composting device.    ADVANTAGE - The continuous high temperature buffer layer and the gas distribution guide plate can be quickly and uniformly realized. The real time storage of the continuous data can be realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the intelligent cabin type aerobic compost device.    Guide folded plate (9)    Hole cover plate (12)    Flow meter (14)    Electromagnetic valve (15)    Air pump (16)    Oxygen monitor (18)    Temperature monitor (19)    Stainless steel bracket (21)    Carbon dioxide monitoring circuit (22)    Ammonia and sulfureted hydrogen monitoring circuit (24)
NOVELTY - A movable composting device comprises movable main control box, monitoring unit, and cover film. The movable main control box has fans, control unit, and ventilation duct.    USE - Movable composting device.    ADVANTAGE - The device is simple and energy-saving, can move at any time according to need of compost site, and has simple implementation process, basic maintenance, low maintenance costs, real-time dynamic control of oxygen, low power consumption, and high processing efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting using movable composting device by connecting fan to ventilation duct, paving on ground, and spreading material; covering with cover film, fixing, monitoring through monitoring unit, and ventilating using fan; and opening cover film, and screening material.
NOVELTY - Method for producing organic fertilizer involves removing debris in wastewater obtained during production of corn starch or wheat starch, adding into sealed container, adding 5-10 wt.% Lactobacillus acidophilus and Saccharomyces cerevisiae in weight ratio of 1:1 to the wastewater, fermenting anaerobically at 30-35 degrees C, stopping fermentation when pH reaches less than 3.5, and adding 3-5 wt.% ferrous sulfate to the fermented product.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The method is simple and cost-effective.
NOVELTY - A mushroom cultivation material comprises 45-55 wt.% wild rice sheath leaves, 10-20 wt.% cottonseed hulls, 15 wt.% sawdust, 14 wt.% wheat bran, 3 wt.% lime powder, 1 wt.% urea, 1 wt.% superphosphate, and 1 wt.% gypsum powder.    USE - Mushroom cultivation material.    ADVANTAGE - The method makes cellulose, hemicellulose and other macromolecules broken down into simpler substances conducive to absorption of mushroom mycelium which promotes growth and has harmless treatment of wild rice sheath leaves. The material has reasonable and balanced nutrition, high yield, and biological efficiency of 138.2-145.1%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of material by cutting wild rice sheath swollen stems and leaves after wild rice harvest, drying, crushing into 2-3 cm long, soaking in lime for 30-36 hours, taking out, and drying; placing two large bamboo on ground, and piling with dried leaves into 1.4-1.5 m high, 2 m wide and unlimited length trapezoidal heap; dissolving urea in water, pouring into heap until completely accumulated, leaking water, covering with straw mats, naturally fermenting, an d inserting 2 m wooden stick while taking out two large bamboo to ensure fermentation quality; and turning heap once every 3 days for total of 3-4 times for 12-15 days, adding gypsum powder/first turning time, adding superphosphate/second turning, and adding cottonseed hulls, sawdust, and wheat bran/last turning time, adding water depending on moisture content of material, and stopping fermentation when moisture content is 63-65%.
NOVELTY - Synthesis of methane gas involves using a system formed by connecting methanol synthesis reactors and methane synthesis reactors in series or parallel, in which methanol synthesis reactor is provided in any location other than the end position.    USE - Synthesis of methane gas and coproduction of methanol (claimed).    ADVANTAGE - The method enables synthesis of methane gas and coproduction of methanol by simple process, under reduced energy consumption.
NOVELTY - Preparation of trifluoromethoxy benzene (f) involves subjecting mixture of benzaldehyde (a) and p-dimethyl benzene (b), and chlorine to chlorination reaction using p-ditrifluoromethylbenzene (c) as reaction solvent, removing the solvent, reacting obtained mixture of ( alpha ),( alpha ),( alpha )-trichloromethyl phenylether (d) and 1,4-bis( alpha , alpha , alpha -trichloromethyl)benzene (e) with anhydrous hydrogen fluoride in presence of perfluoro sulfonyl fluoride-type catalyst, and performing fluorination reaction to obtain trifluoromethoxy benzene and p-bis(trifluoromethyl)benzene (g).    USE - Preparation of trifluoromethoxy benzene (claimed).    ADVANTAGE - The trifluoromethoxy benzene is safely prepared by environmentally-friendly and simple method.    DETAILED DESCRIPTION - Preparation of trifluoromethoxy benzene of formula (f) involves subjecting benzaldehyde of formula (a) or mixture of benzaldehyde (a) and p-dimethyl benzene of formula (b) as raw material, and chlorine to chlorination reaction using p-ditrifluoromethylbenzene of formula (c) as reaction solvent, and phosphorus trichloride, azobisisobutyronitrile and/or benzoyl peroxide as initiator to obtain mixture of ( alpha ),( alpha ),( alpha )-trichloromethyl phenylether of formula (d) and 1,4-bis( alpha , alpha , alpha -trichloromethyl)benzene of formula (e), removing the solvent, reacting mixture of ( alpha ),( alpha ),( alpha )-trichloromethyl phenylether (d) and 1,4-bis( alpha , alpha , alpha -trichloromethyl)benzene (e) with anhydrous hydrogen fluoride in presence of perchloro sulfonyl fluoride-type catalyst, and performing fluorination reaction to obtain trifluoromethoxy benzene (f), and p-bis(trifluoromethyl)benzene of formula (g) as byproduct. The byproduct can be added during chlorination process.
NOVELTY - Salicylic acid, acetone, and potassium hydroxide are stirred at room temperature. Bromoethane is dripped, and the mixture is heat-refluxed for 9-15 hours, decompressed, and filtered to recycle acetone. Water and liquid alkali are added, and the reaction mixture is heat-refluxed for 2-4 hours, cooled to room temperature, pH-adjusted to 3-4, cooled to 1-15 degrees C, and filtered. The separated residue is water-washed and vacuum-dried to obtain o-ethoxybenzoic acid. The ratio of salicylic acid, potassium hydroxide, bromoethane, and liquid alkali is 1:2:2.1:1.    USE - Synthesis of o-ethoxybenzoic acid (claimed).    ADVANTAGE - The method enables simple and convenient industrial synthesis of o-ethoxybenzoic acid with high yield and quality, using economical raw materials.
NOVELTY - Production of tertiary amine ester involves adding the fatty acid and ethanol amine in the molar ratio of 1.7-2:1, adding 0.1 wt.% solid acid catalyst to the reactant, adding the fatty acid in the reactor, stirring and raising temperature after completely melted, then adding ethanolamine and solid acid catalyst in nitrogen atmosphere, operating temperature, reducing the product acid value to 3 mg potassium hydroxide/g, stopping the reaction, performing the temperature of reaction system and hot filtering the solid acid catalyst.    USE - Production of tertiary amine ester (claimed).    ADVANTAGE - The tertiary amine ester is efficiently prepared with high catalytic activity, and excellent selectivity without polluting the environment.    DETAILED DESCRIPTION - Production of tertiary amine ester involves adding the fatty acid and ethanol amine in the molar ratio of 1.7-2:1, adding 0.1 wt.% solid acid catalyst to the reactant, adding the fatty acid in the reactor, stirring and raising temperature after completely melted, then adding ethanolamine and solid acid catalyst in nitrogen atmosphere, operating temperature at 170-200 degrees C, performing esterification reaction under nitrogen atmosphere, reducing the product acid value to 3 mg potassium hydroxide/g, stopping the reaction, performing the temperature of reaction system at 70 degrees C and hot filtering the solid acid catalyst.
NOVELTY - Preparation of 4-epitetracycline involves adding tetracycline urea complex salt crystal mother solution with oxalic acid to adjust the pH value of 1-3 at 25-40 degrees C, stirring for 10-40 minutes by double layer 621 filter cloth, filtering, reducing the obtained filtrate at 18-22 degrees C, evenly and slowly adding into the aqueous ammonia until the pH value of 4-6, controlling the temperature at 5-20 degrees C, stirring for 60-120 minutes, crystallizing, separating, washing and dehydrating.    USE - Preparation of 4-epitetracycline (claimed).    ADVANTAGE - The 4-epitetracycline is efficiently prepared with reduced environmental protection.
NOVELTY - A sulfonated polyether-ether-ketone/amino-functionalized titania hybrid membrane has sulfonated polyether-ether-ketone/amino-functionalized titania hybrid film having thickness of 60-80 microns and containing polyether ether ketone and amino-functionalized titania microspheres in mass ratio of 0.85-0.95:0.15-0.05 and sulfonation degree of 72.8%.    USE - Sulfonated polyether-ether-ketone/amino-functionalized titania hybrid membrane is used for separating carbon dioxide/methane mixture (claimed).    ADVANTAGE - The sulfonated polyether-ether-ketone/amino-functionalized titania hybrid membrane is prepared under mild reaction conditions, by simple method. The carbon dioxide/methane mixture is separated with selectivity of 33-48 and permeability of 75-1253 barrer, using the sulfonated polyether-ether-ketone/amino-functionalized titania hybrid membrane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sulfonated polyether-ether-ketone/amino-functionalized titania hybrid membrane, which involves adding amino-functionalized titania microspheres to trihydroxymethyl aminomethane-hydrogen chloride solution, stirring at room temperature, reacting for 24 hours, centrifuging and separating, washing filter cake with ethanol and drying to form modified titania, adding modified titania to 5% aqueous solution of polyethylene imine, reacting at 65 degrees C for 24 hours, cooling, centrifuging and separating, washing filter cake with ethanol and drying to obtain amino-functionalized titania, stirring sulfonated polyether-ether-ketone in 72.8% N,N-dimethylacetamide as solvent, ultrasonically dispersing amino-functionalized titania in resulting mixture, defoaming, casting and drying mixture.
NOVELTY - The device has a feeding pipe (4) that is connected with an inner flange (9) and an outer flange (6) through a bolt (5). The inner flange is provided with an oil injection adjusting bolt (8) which is press-contacted with a roller adjusting ring (22). A roller (15) is provided with a packing strip (7), a spiral groove plate (25) and a transverse rod (11). The transverse rod is connected with a hanging rod (12) which is connected with several electric heating coils (14). The electric heating coil is coated on the roller, and covered with an insulating layer (13).    USE - Biomass pyrolysis and gasification device.    ADVANTAGE - Since the energy consumption of the biomass pyrolysis and gasification device is decreased, the enterprise production cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass pyrolysis and gasification device.    Feeding pipe (4)    Bolt (5)    Outer flange (6)    Packing strip (7)    Oil injection adjusting bolt (8)    Inner flange (9)    Transverse rod (11)    Hanging rod (12)    Insulating layer (13)    Electric heating coil (14)    Roller (15)    Roller adjusting ring (22)    Spiral groove plate (25)
NOVELTY - The device has an electric heater (9) which is connected to carbon powder burner (7). The burner is connected to heat exchanger (8). The heat exchanger is connected to pyrolysis reactor (1). The pyrolysis reactor is connected with two-stage series cyclone separator (2). The inlet of discharge valve (5) is connected with water cooling jacket of spiral conveying machine (6). The spiral conveying machine is connected with burner. The integrated biological oil condenser (3) is connected to bio-oil tank (4). The bio-oil tank is connected to exchanger. The heater is connected to reactor.    USE - Forest and agricultural waste thermal pyrolysis device.    ADVANTAGE - The heat-exchanging of hot flue gas and non-condensable gases can be performed easily and effectively by using the heat exchanger. The heated non-condensable gas is introduced into a fluidized bed pyrolysis unit. The reliability of the pyrolysis device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the forest and agricultural waste thermal pyrolysis device.    Pyrolysis reactor (1)    Two-stage series cyclone separator (2)    Biological oil condenser (3)    Bio-oil tank (4)    Discharge valve (5)    Spiral conveying machine (6)    Carbon powder burner (7)    Heat exchanger (8)    Electric heater (9)
NOVELTY - The method involves crushing plant raw materials. Sieving process and drying process are carried out for crushed materials. An alcohol solvent i.e. methanol and ethanol/isopropanol, is added in a high pressure reaction kettle. Solid heteropoly acid i.e. phosphotungstic acid, phosphorus key acid/zirconium phosphate acid, is made to react with a catalyst substance for 10-50 min in an ultra-critical state. A liquefied product is selected as absolute ethyl alcohol. Filtering process and rotary steaming process are performed. Biomass oil is filled in a rotary steaming container.    USE - Plant raw material ultra-critical fluid catalyzing and liquefying method.    ADVANTAGE - The method enables avoiding toxic effect and ensuring high lubricity effect and high heat value.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating a plant raw material ultra-critical fluid catalyzing and liquefying method.
NOVELTY - Preparation of tung oil biodiesel involves immersing porous inorganic material as carrier in 7-12 %mass heteropolyacid solution, drying, roasting and cooling, then immersing in salt solution comprising cobalt, iron, nickel and tungsten, baking and cooling to obtain catalyst, subjecting obtained catalyst to reduction process at 400-420 degrees C for more than 5 hours, introducing hydrogen gas, then adding tung oil and performing hydrogenation cracking reaction at 340-420 degrees C.    USE - Preparation of tung oil biodiesel (claimed).    ADVANTAGE - The method enables preparation of tung oil biodiesel with high quality by environmentally-friendly and simple process.
NOVELTY - The furnace has a feeding device provided with a feeding box (1), a vent-pipe (2) and a fan (3). The vent-pipe is fixed with the feeding box. The vent-pipe and the fan are connected with a reaction chamber (4) that is sleeved with an outer side of an air storage tank (5). An output end of the reaction chamber is connected with an input end of a gasification chamber (6). The reaction chamber is provided with an air inlet (8). An air compensating pipe (14) is connected with the gasification chamber that is connected an output end of a hearth heat receiver (12).    USE - Secondary-clean burning biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure and environment-friendly, and improves utilization rate of biomass particles and reduces water gas pollution caused by biomass particle combustion.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a secondary-clean burning biomass gasification furnace.    Feeding box (1)    Vent-pipe (2)    Fan (3)    Reaction chamber (4)    Air storage tank (5)    Gasification chamber (6)    Air inlet (8)    Hearth heat receiver (12)    Air compensating pipe (14)
NOVELTY - The method involves crushing and drying raw material. Raw material particle size diameter is less in 5 mm. A water content index of the raw material is controlled for about less than 20%. A high-efficiency gasification furnace is arranged in a horizontal circulating fluidized bed system.    USE - Siloxane organic silicon hydrolysate gasification method.    ADVANTAGE - The method enables improving electricity generating efficiency and biomass conversion efficiency, reducing water wastage rate and steam pressure and preventing environment from being polluted.
NOVELTY - The furnace has a stainless steel plate connected with a central pipe (7) by a gas collecting pipe (9). An aeration pipe (6) is arranged with a vertical hot-resistant steel cylinder that is formed with a hot insulating layer (17). A tar cracking chamber (20) is formed with a carbide combustion reducing layer that is filled with waste matter by an ash layer (24). A pan (25) is fixedly connected with a furnace body. A gasification agent inlet (26) is filled with gasification agent. The stainless steel plate is vertically connected with the gas collecting pipe.    USE - Dioxin-free anti-gas emission rubbish dry-gasification furnace.    ADVANTAGE - The furnace is simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a dioxin-free anti-gas emission rubbish dry-gasification furnace.    Aeration pipe (6)    Central pipe (7)    Gas collecting pipe (9)    Hot insulating layer (17)    Tar cracking chamber (20)    Ash layer (24)    Pan (25)    Gasification agent inlet (26)
NOVELTY - Animal and vegetable fats, methanol, mixed aromatic hydrocarbons, surfactant, methyl tertiary butyl ether, amine and diesel oil are stirred in a reactor at 40-65 degrees C for 20-50 minutes, to obtain composite biodiesel.    USE - Preparation of composite biodiesel used in compression ignition engines, fuel boilers and industrial furnaces.    ADVANTAGE - The method enables preparation of clear and bright composite biodiesel with excellent durability, solubility and dynamic property by simple process.
NOVELTY - A diesel oil reversed micelle system comprises 30-75 g/L rhamnolipid, diesel oil, 15-60 g/L co-surfactant and 24-30 mg/L water.    USE - Diesel oil reversed micelle system is used for preparing biodiesel (claimed).    ADVANTAGE - The diesel oil reversed micelle system is prepared by simple process. The biodiesel is efficiently prepared by environmentally-friendly and simple process without changing the chemical structure of the castor oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of diesel oil reversed micelle system, which involves dissolving rhamnolipid in diesel oil, then adding co-surfactant and excess of water, aging and separating;    (2) biodiesel oil, which comprises 80-95 volume% diesel oil reversed micelle system and 5-20 volume% castor oil; and    (3) preparation of biodiesel, which involves mixing diesel oil reversed micelle system and castor oil, maintaining at predetermined temperature, centrifuging and separating.
NOVELTY - A crop straw briquette comprises 30-70 wt.% crop straw and 30-70 wt.% charcoal.    USE - Crop straw briquette (claimed).    ADVANTAGE - The crop straw briquette having high quality is prepared.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of crop straw briquette, which involves mixing pulverized crop straw with length of 3-7 mm and pulverized charcoal with particle diameter of 0.1-3 mm, adjusting water content of the mixture to 11-15%, and extruding.
NOVELTY - Preparation of biofuel involves pretreating raw material, removing the impurities contained in the raw material, crushing, drying, performing steam explosion and solid-liquid separation, washing and pressing.    USE - Preparation of biofuel (claimed).    ADVANTAGE - The biofuel with high quality is economically produced by simple method using waste biomass including animal and plant waste, agricultural and forestry waste and municipal solid waste.
NOVELTY - An additive contains 8-15 wt.% calcium oxide, 5-8 wt.% iron oxide, 6-10 wt.% magnesium hydroxide, 10-15 wt.% calcium carbonate, 35-45 wt.% activated carbon, 20-25% wooden flour and 2-5 wt.% manganese dioxide.    USE - Additive for improving calorific value of solid waste derived fuel.    ADVANTAGE - The additive effectively improves calorific value of solid waste derived fuel, and is economically prepared.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of additive.
NOVELTY - Cracking method of biomass involves thermal decomposition gasification of biomass, obtaining combustible mixed gas, performing catalytic process with high molecular weight of hydrocarbon at 890-1200 degrees C in presence of catalyst, obtaining carbon molecular gas, reacting at 920-990 degrees C, performing hot decomposition process under biomass anaerobic condition, removing dust and discharging, drying, and purifying. The catalyst is ferric oxide, copper oxide, zinc oxide or magnesium oxide. The biomass is wood, wild grass plant, crop straw or waste residue.    USE - Cracking method of biomass (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for performing cracking method of biomass, which has feeding port, exhaust port, and combustion chamber.
NOVELTY - Method for preparing liquid organic fertilizer, involves (a) obtaining kitchen garbage as raw material, and separating mixed inorganic and organic components of kitchen garbage, (b) adding the organic component into fermentation chamber with small amount of saw dust, adding mixed flora, and fermenting the mixture after decomposition of kitchen garbage, and (c) liquefying the fermented mixture through conveying pipe, and performing deployment process to obtain product in fertilizer preparing box.    USE - The method is useful for preparing liquid organic fertilizer (claimed).    ADVANTAGE - The method is cost-effective, consumes less energy, enables short production period, and utilizes waste resource.
NOVELTY - The device has a stirring device (3) that is provided with a stirring blade (8) and main shaft (9). A pushing device (4) is provided with a spiral shaft (12) and arched channel provided corresponding to size of spiral packing auger (10). The spiral packing auger is fixed in screw shaft centre of spiral auger device, and one side of fermentation tank (5) is equipped with a feed port (15). Surface of fermentation device is provided with a heating device, and driving mechanism is provided for driving the pushing device and stirring device.    USE - Integrated type garbage fermentation device.    ADVANTAGE - Integrated type garbage fermentation device is featured with simple structure, large amount of manpower and material resources can be saved, and manufacturing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated type garbage fermentation device.    Stirring device (3)    Pushing device (4)    Fermentation blade (5)    Stirring blade (8)    Spiral packing auger (10)    Spiral shaft (12)    Feed port (15)
NOVELTY - The device has a battery power supply (31), a first filter (32), an oscillator (33), step-down transformer (34), rectifier (35), a second filter (36), a voltage stabilizer (29), and current-limiting machine (30). The hydrogen making machine is equipped with electrode group (8) composed of several electrode plate (28). The electrode plate is connected with cathode of the current limiter. Anode of current limiter and the electrode plate are connected with the cathode of the current limiter. The odd electrode plate is connected adjacent with the even electrode plate.    USE - Hydrogen production device for vehicle.    ADVANTAGE - The combustion efficiency of the device can be improved. The structure of the hydrogen production device can be simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen production device. (Drawing includes non-English language text)    Electrode group (8)    Electrode plate (28)    Voltage stabilizer (29)    Current-limiting machine (30)    Battery power supply (31)    First filter (32)    Oscillator (33)    Step-down transformer (34)    Rectifier (35)    Second filter (36)
NOVELTY - The machine has power supply (1), first filter (2), an oscillator (3), step-down transformer (4), rectifier (5), second filter (6), voltage stabilizer (7), and electrode group that are arranged on electrode plate (10). The battery power supply is connected with first filter, oscillator, boosting device, rectifier, second filter, voltage stabilizer and current-limiting device. Anode of odd electrode plate current-limiting device is connected with a cathode respectively. The odd electrode plate is connected with even odd electrode plate and are provided adjacent with each other.    USE - Hydrogen production machine for vehicle.    ADVANTAGE - The combustion efficiency of the machine can be improved. The power consumption can be reduced. The operating performance of the machine can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen production machine. (Drawing includes non-English language text)    Power supply (1)    First filter (2)    Oscillator (3)    Step-down transformer (4)    Rectifier (5)    Second filter (6)    Voltage stabilizer (7)    Electrode group (10)
NOVELTY - This utility model claims one kind of special purifying residual particles, having an amino acid, Chinese medicinal herb layer is coated with said amino acid, taurine layer, layer humic acid and plant protein layer, a stabilizer layer between the said layer and humic acid layer, a polysaccharide-iron composite layer between the said layer humic acid and plant protein layer. This utility model aims at the characteristics of livestock breeding in livestock cultivation, Chinese herbal medicine, amino acid, taurine and other nutrient substances as food additive, so that in normal animal feed in a more nutrient element, increasing immunity, at the same time, it can remove heavy metal in an animal residual harmful substances.
NOVELTY - The method involves remaining portion of metallic cobalt layer to oxidize conditions for predetermined time and temperature, so that surface portion of cobalt layer is oxidized to cobalt oxide. An electrically conductive interconnect (28) is comprised of metallic cobalt layer sandwiched between a surface layer of cobalt oxide and a layer of cobalt-iron-chromium alloy. A substrate made of iron-chromium alloy is sandwiched between two fuel cells. Two surfaces (28a,28b) of substrate is in electrical contact with anode (16) and cathode (18) of two fuel cells respectively.    USE - Method of manufacturing solid oxide fuel cell stack.    ADVANTAGE - The layer of metallic cobalt or cobalt oxide is highly effective in preventing formation of chromium oxide and other related species and subsequent detrimental reaction with the cathode. The resulting surface is provided with high electrical conductivity that is stable over extended time in high temperature operating environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the two-cell stack of solid oxide fuel cells.    Solid oxide fuel cell stack (10)    Anode (16)    Cathode (18)    Electrically conductive interconnect (28)    Surfaces of substrate (28a,28b)
NOVELTY - The fuel cell system has a fuel cell stack (300) that allows electricity in a reformed fuel that is preheated with the heat of combustion generated in a catalytic combustor (200). A fuel reformer (100) having the generated heat of combustion as the heating source in the catalytic combustor. The catalytic combustor burns the fuel supplied from a fuel feeder (50). The catalytic combustor is the fuel cell stack that puts the fire fuel as temperature rises due to generation of electricity. The fuel reformer includes the reformer that generates a reformate gas fuel.    USE - Fuel cell system equipped in a vessel.    ADVANTAGE - The fuel cell stack allows electricity in a reformed fuel preheated with the heat of combustion generated in a catalytic combustor and the fuel reformer having generated heat of combustion as heating source in the catalytic combustor, thus reduces the catalytic combustor energy and the warm-up time in a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system. (Drawing includes non-English language text).    Fuel feeder (50)    Fuel reformer (100)    Back up reformer (110)    Catalytic combustor (200)    Fuel cell stack (300)
NOVELTY - The aircraft (10) has a hydrogen-containing envelope (20), an electrolyzer (30) to convert water into hydrogen and a hydrogen-replenishment system for replenishing the envelope with hydrogen generated using the electrolyzer. The water-collection system collects water from the envelope for use by the electrolyzer. The envelope comprises a non-rigid wing-shaped inflatable structure.    USE - Aircraft such as a hydrogen-regenerating solar-powered aircraft, hydrogen-fuelled aircraft (claimed). Uses include but are not limited to hybrid aircraft, an airship, air-based or airborne station, air vehicle. Can also be used for flying boat or other flying machine or apparatus that uses hydrogen as a lifting gas.    ADVANTAGE - Provides an aircraft having a hydrogen-regenerating capability to regenerate and thus replenish hydrogen gas for the aircraft. The on-board production of hydrogen enables automatic top-ups of hydrogen when required, which renders the aircraft fully self-reliant and self-sufficient when working in remote areas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for hydrogen-fuelled aircraft.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an all-hydrogen aircraft.    Aircraft (10)    Hydrogen-containing envelope (20)    Hydrogen gas cells (24)    Hydrogen manifold (26)    Electrolyzer (30)
NOVELTY - Pellets and briquettes made of peanut shells, are claimed.    USE - Used as pellets and briquettes.    ADVANTAGE - The pellets and briquettes: has peanut shell having a large energy value; and can be prepared without generating charcoal, thus they are environmental friendly.
NOVELTY - The utility model claims an organic fertilizer production processing field, claims one kind of organic fertilizer production complete automation device, comprising a fertilizer storage tower, mixing, stacking and fermenting organic fertilizer. The utility model claims each flow of the organic fertilizer production complete automation device, the organic fertilizer production, reduces the cost and improves the production efficiency, in the process of turning, using a high-pressure fan, the oxygen-increasing and temperature-reducing effect.
NOVELTY - This utility model claims one kind of plant for purifying pesticide residue instant granule, comprising curing organic fertilizer ball, ellipsoid structure is the plant fibre in the said curing organic fertilizer ball are coated with water absorbing silicon glue layer, a Chinese medicinal herb layer and polymer release layer on the outer side of the said plant fibre body is coated with calcium carbonate powder layer is set on the outer side of the said polymer release layer is coated with a colouring agent layer is set on the outer side of the said calcium carbonate powder layer is covered at the outer side of said grass colorant layer. The structure of this utility model is simple, the design is reasonable, the quality of the plant for the pollution problem of soil compaction and soil environment, improving the soil water-absorbing energy, curing heavy metal residue, can effectively improve the quality of the soil, improves soil, ability, increase organic soil, so as to improve the soil planting.
NOVELTY - A cetylpyridinium chloride is prepared by mixing chlorohexadecane and pyridine, heating the mixture at 100-125 degrees C for 10-14 hours, decompressing, adding alcohol solvent and activated carbon to decolor, reflux heating for 20-50 minutes, cooling, crystallizing, filtering, mixing filtrate and pyridine chloride at a ratio of 1:1-15, adding water and acetone, heating, cooling to form crystals, filtering, mixing ethanol and acetone, adding filter cake to the solution at a ratio of 1:1-15, heating, cooling, and refining.    USE - Method of preparing cetylpyridinium chloride (claimed).    ADVANTAGE - The method is simple and easy to control, has mild reaction condition and reduced energy consumption, and can be easily applied to industrial production.
NOVELTY - Composting of forest industry solid waste comprises mixing 1/2-3/4 forest industry solid waste and 1/4-1/2 manure to a water content of 45-60%, and carbon-nitrogen ratio of 20-30:1; spreading mixture on ground, piling at a bottom width of 4 m, top width of 1-1.5 m and height of 2 m, decomposing for 18-20 days; and curing decomposed fertilizer for 2 weeks.    USE - Method for composting forest industry solid waste used for producing fertilizer (claimed).    ADVANTAGE - The prepared fertilizer improves physical performance of soil by softening, increases water-retaining property, air permeability and water permeability, and enhances absorption, growth and cultivation of plant root.
NOVELTY - Organic fertilizer and its preparation method, are claimed. The organic fertilizer comprises 9-13 pts. wt. rotten fruit, 12-16 pts. wt. twig weeds, 11-15 pts. wt. corn, 7-14 pts. wt. peanut shell, 3-8 pts. wt. black mica, 3-8 pts. wt. perlite, 3-8 pts. wt. medical stone, 12-16 pts. wt. humus, 0.7-1.3 pts. wt. organic material fermenting agent, and 3-7 pts. wt. sugar beet.    USE - The organic fertilizer is useful for rapeseed (claimed) for improving soil structure, and reducing plant diseases caused by insect pests.    ADVANTAGE - The organic fertilizer can provide a large amount of plant growth nutrient elements, can improve rapeseed yield, reduces the requirement of additional fertilizer, and provides everlasting effect.    DETAILED DESCRIPTION - Organic fertilizer and its preparation method, are claimed. The organic fertilizer comprises 9-13 pts. wt. rotten fruit, 12-16 pts. wt. twig weeds, 11-15 pts. wt. corn, 7-14 pts. wt. peanut shell, 3-8 pts. wt. black mica, 3-8 pts. wt. perlite, 3-8 pts. wt. medical stone, 12-16 pts. wt. humus, 0.7-1.3 pts. wt. organic material fermenting agent, and 3-7 pts. wt. sugar beet. The fertilizer is prepared by crushing twig weed, corn and peanut shell using a crusher, adding humus and rotten fruit, uniformly mixing, performing fermentation at 40-55 degrees C for 24-48 hours, adding the black mica, perlite, medical stone and sugar beet, and uniformly mixing to obtain the product.
NOVELTY - Plant fertilizer comprises 10-15 pts. wt. straw, 20-30 pts. wt. powdered rock phosphate, 15-18 pts. wt. organic acid, 10-12 pts. wt. potassium chloride, 3-5 pts. wt. trace element, 5-6 pts. wt. calcium sulfate, 1-3 pts. wt. growth regulator, and 10-15 pts. wt. yellow phosphorus slag.    USE - Used as a plant fertilizer.    ADVANTAGE - The fertilizer comprises natural straw raw material, which greatly improves fertilizer effect, and reduces the pollution to the environment; is simple to manufacture, does not produce pollution to the environment in the production process; and makes the soil fertile, and effectively reduce the soil pH value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing plant fertilizer, comprising (i) adding the straw into a crusher to crush, then adding growth regulator, organic acid and potassium chloride, stirring and mixing uniformly, placing in a sealed container to ferment to obtain the fermentation product, where the fermenting time is 20-30 hours, and (ii) drying yellow phosphorus slag, then grinding, adding powdered rock phosphate, trace element and calcium carbonate, stirring and mixing uniformly, adding fermentation product obtained in the step (i), and stirring to obtain the fertilizer.
NOVELTY - Microbial complex fertilizer comprises microbial agent, composted straw powder, urea, potassium chloride and diatomite.    USE - The microbial complex fertilizer is useful in crop cultivation (claimed).    ADVANTAGE - The fertilizer: is environmentally friendly (claimed); improves hardening of soil, improves utilization rate of fertilizer, improves crop yield by achieving the standard of green food product; utilizes microorganism which inhibit the occurrence of plant diseases and insect pests; reduces the utilization of farm chemicals; and achieves food safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of microbial complex fertilizer in crop cultivation.
NOVELTY - Producing fertilizer useful for saline-alkali soil comprises (i) crushing alfalfa grass and comfrey, mixing with corn cob powder, then stirring uniformly with pig manure, inoculating with fermentation bacteria, composting to height of 30-50 cm, covering with a plastic film cover and fermenting for 10-12 days, and (ii) adding cation exchange resin into fermentation product, adding nitrogen-fixing bacteria and polyacrylamide, watering until the moisture content is 6365%, preparing into bar-shape by an extruder, and drying to obtain 5-8 cm fertilizer bar.    USE - The fertilizer is useful for saline-alkali soil (claimed).    ADVANTAGE - The method is simple. The fertilizer has simple composition, is convenient to use, reduces salt content in the soil, enhances activity of soil microorganism and enzyme, and promotes growth of plant root.
NOVELTY - A Phenethacillin is prepared by placing penicillin sodium or penicillin potassium in organic solvent, reacting penicillin sodium or penicillin potassium and 2-chloro-triethylamine or 2-chloro-triethylamine hydrochloride at 20-80 degrees C, removing organic solvent and sodium chloride or potassium chloride, and acidifying.    USE - Method for preparing Phenethacillin (claimed).    ADVANTAGE - The method shortens the process step, directly avoids toxicity of ethyl chloroformate, which reduces cost of processing and pollution to the environment, and improves reaction yield to 80-90%.
NOVELTY - Organic lithium gasoline antidetonant comprises 1-5 pts. wt. organic lithium and auxiliary agent containing 85-95 pts. wt. methanol, 1-15 pts. wt. toluene and 1-5 pts. wt. isopropanol.    USE - Organic lithium gasoline antidetonant used in automobile engine.    ADVANTAGE - The antidetonant increases gasoline octane value and improves gasoline combustion performance, removes combustion residue, reduces waste gas emission, and used in automobile engine with no adverse effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic lithium gasoline antidetonant comprising mixing organic lithium and auxiliary agent at room temperature under normal pressure to obtain product.
NOVELTY - Wet absorption of carbon dioxide comprises mixing the carbon dioxide with an alkali metal hydroxide dissolved in an ethanol to obtain an alkali metal ethylcarbonate.    USE - The method is useful for wet absorption of carbon dioxide to synthesis sodium ethylcarbonate or potassium ethylcarbonate for preparing ethanol that is used as a fuel (all claimed), where the carbon dioxide generated a heat power plant, an iron mill, and in a petrochemical and cement industries.    ADVANTAGE - The method is capable of preparing ethanol in a simple and environment-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing sodium ethylcarbonate or potassium ethylcarbonate including injecting the carbon dioxide gas or carbon dioxide mixing gas with sodium hydroxide or potassium hydroxide dissolving the in ethanol to obtain sodium ethylcarbonate or potassium ethylcarbonate, where the mixture has a concentration of 0.05-3.5 M; and    (2) preparing ethanol including dissolving the solid alkali metal ethylcarbonate in water.
NOVELTY - The device (1) has processing device (10) that crushes the organic waste, and the liquid feed pump (19) transfers the organic waste to liquid storage tank (16). The leachate is generated in the dehydrator (13). A crashing-separator (11) is provided with the adulteration reservoir (14), while transferring organic compound from crashing-separator. A crushed material feed pump (12) transfers organic compound selected with the crashing-separator to the dehydrator. A product reservoir (18) receives the dehydration cake separated from the operating procedure of the dehydrator.    USE - Device for treating and recycling organic waste, installed in separate wastewater disposal facilities.    ADVANTAGE - The process efficiency of the organic waste can be increased with the processing device, by recycling the dehydration cake and dehydration filtrate of the organic waste. The economical adulteration and dehydration filtrate are separated using the transfer apparatus of the processing device. The maintenance management cost of the recycling device can be decreased. The reduction of consumption of energy can be achieved and the occurrence of bad smell in processing device can be prevented. The burning of the supply of medicines problem for the wastewater treatment can be prevented. The chemical expense at the combustion process can be s saved by converting the effluent of the high concentration generated in the pre-processing of organic waste. The maintenance cost of the energization apparatus is minimized by converting the sewage sludge. The handling cost of the organic waste can be minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the device for treating and recycling organic waste.(Drawing includes non-English language text)    Device for treating and recycling organic waste (1)    Processing device (10)    Drying fuel recycling facility (20)    Process manufacturing facility (30)
NOVELTY - The device has gross and card channels which are arranged perpendicularly to each other. A main portion is located on mineral ground. The gross channels, card channels and drains are covered with the layer of material filler. The drains are cut parallel to the card channels and are provided with side of gross channels. The layer of filled ground is provided on surface of card. Thickness of filled ground is evenly distributed over the shaped surface of field. The card channels are arranged in parallel to each other.    USE - Device for laying and drying of lump fuel peat.
NOVELTY - Nutritional supplement comprises fungal biomass having at least 100 mg/kg iron.    USE - As nutritional supplement.    ADVANTAGE - The supplement is cost-effective and suitable for animal or human consumption, and utilizes fungal biomass obtained from fungi that have generally recognized as safe (GRAS) status and have ability to accumulate organic iron from natural sources such as agricultural and food process wastes and by-products without iron fortification when such wastes and by-products are used as a growth media.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for forming a nutritional supplement containing iron, involves culturing filamentous fungi in an agricultural by-product or a food processing by-product to accumulate iron in the filamentous fungi present in the agricultural or food processing by-product, and harvesting the filamentous fungi to form a nutritional supplement containing fungal biomass having at least 100 mg/kg iron; and    (2) nutritional supplement containing iron prepared by the above-mentioned method.
NOVELTY - The apparatus provides fermentation vapor to upper portion of organic recycled materials to be isolated into air and liquid. The isolated air is returned in fermenter (1) and is circulated into airtight fermenter through organic recycled material. Multiple air supply pipes (5) are parallely arranged with predetermined spacing in the under-floor of fermenter. The air flow amount adjusting device (5a-5e) is set with air supply pipe, so that the air flow amount flowing into air supply pipe with air flow amount adjusting device is adjusted.    USE - Ripening soil formation apparatus.    ADVANTAGE - The carrying out of organic waste to stir from fermenter during middle time of ripening soil formation process becomes unnecessary, thus the ripening soil can be made effectively. The ripening soil can be formed with rich biodiversity activity. The formation of ripening soil can be made effectively without causing any replant failure. The coexisting of aerobe and anaerobic bacteria in the ripening soil can be generated.    DETAILED DESCRIPTION - The opening and closing of fermenter is made to ensure airtightness. The fermented microorganisms in organic waste (6) are thrown in the fermenter. The fermenter is sealed for fermenting thrown-in organic waste to produce microorganism fermented compost. The organic recycled materials are inserted in the microorganism phase in fermenter. The air is circulated from lower portion of the organic recycled materials for fermenting organic waste in the organic recycled material. The flow measurement unit is set with air supply pipe, so that the air flow amount of air supply pipe is equal by the flow volume adjustment unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the ripening soil formation apparatus.    Fermenter (1)    Air supply pipe (5)    Air flow amount adjusting devices (5a-5e)    Organic waste (6)    Air supply blower (11)
NOVELTY - Method for enhancing enzymatic hydrolysis of lignocellulose biomass involves (a) providing an aqueous dispersion of biomass, (b) adding prepared fungal laccase to the biomass, (c) adding prepared one or more of cellulose hydrolyzing enzyme to the biomass (b), where the addition in step (b) is either simultaneous with the addition in step (c), or before addition in step (c), and (d) incubating the biomass of step (b) and step (c) either simultaneously or in sequence.    USE - The method is useful for enhancing enzymatic hydrolysis of lignocellulose biomass using enzyme composition in the form of dry powder, dry tablet or liquid. The enzyme composition is useful for enhancing cellulase-mediated hydrolysis of lignocellulose biomass (all claimed).    ADVANTAGE - The method enhances yield of fermentable sugar from biomass.    DETAILED DESCRIPTION - Method for enhancing enzymatic hydrolysis of lignocellulose biomass involves (a) providing an aqueous dispersion of biomass, (b) adding prepared fungal laccase to the biomass, (c) adding prepared one or more of cellulose hydrolyzing enzyme to the biomass (b), where the addition in step (b) is either simultaneous with the addition in step (c), or before addition in step (c), and (d) incubating the biomass of step (b) and step (c) either simultaneously or in sequence, where the fungal laccase is a polypeptide having at least 85% amino acid sequence homology to SEQ ID NO: 5 (sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication). An INDEPENDENT CLAIM is included for enzyme composition, which comprises fungal laccase, where the laccase is a polypeptide having at least 85% amino acid sequence homology to SEQ ID NO: 5.
NOVELTY - The furnace (1) has a combustion furnace unit (2) and a carbonization furnace unit (3) that are arranged integrally and adjacently. A combustion chamber (5) of combustion furnace unit is connected to a heating chamber (6) of carbonization furnace unit. A gas emission unit (24) is provided in predetermined location of carbonization furnace unit, to release gas accumulated in combustion chamber of combustion furnace unit or heating chamber of carbonization furnace unit.    USE - Organic substance carbonization and combustion furnace for carbonizing and combusting foodstuff waste material, wood material, industrial waste material, animal excrement and bamboo material.    ADVANTAGE - The waste material having organic substance can be processed more efficiently, while suppressing the generation of the toxic substance of odor or dioxins. The compactization of carbonization and combustion furnace can be attained by integrally comprising combustion furnace unit and carbonization furnace unit. Since the temperature of the furnace wall around carbonization furnace unit is heated more equally, the carbonization efficiency and combustion stabilization of carbonization and combustion furnace can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of organic substance carbonization and combustion furnace.    Organic substance carbonization and combustion furnace (1)    Combustion furnace unit (2)    Carbonization furnace unit (3)    Combustion chamber (5)    Heating chamber (6)    Gas emission unit (24)
NOVELTY - The electric power system has a power generator that supplies electricity to a demanding place connected to a fuel cell power generating device. Another power generator supplies the electricity for running the fuel cell power generating device. A supplementary power generator produces the electricity, which is blocked with an outside power source. A fuel cell stack generates the electric power through the electrochemical reaction of fuel and oxidizing agent. A distribution panel supplies electricity to the demanding place. The supplementary power generator produces electricity by fossil fuel.    USE - Electric power system, such as a stand-alone electric power system.    ADVANTAGE - The electric power system has a power generator that supplies electricity to a demanding place connected to a fuel cell power generating device, and thus generates electric power independently without connected to the power supply facility, enable to provide the power demand place of small medium-size, and provides high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an electric power system. (Drawing includes non-English language text).
NOVELTY - The fuel cell operating system has an electric heater (110) that applies heat in a fuel cell stack (100) which is capable of producing an electro chemical reaction of fuel, air electricity and water. A control unit stops fuel supply to the fuel cell stack if more power is generated in an electric power system supplying electricity of being produced in mechanical balance of plant (MBOP) (200) to feed air. An electric power converting section (310) supplies a portion of electricity produced in the fuel cell stack to a fan (280) for the nitrogen purging and electric heater.    USE - System for operating fuel cell such as molten carbonate fuel cell and solid oxide fuel cell.    ADVANTAGE - The high temperature state of the fuel cell stack is maintained in EBOP or the system in the abnormal occurrence. The immediate cool-down is delayed. The lifetime of the fuel cell stack can be prevented from shortening. High temperature state maintenance and nitrogen purging can be performed. The normal termination of the fuel cell stack is possible by controlling the safe cooling rate so that the fuel cell stack is not overstressed from the situation as long as the cool-down has to be performed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fuel cell operation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell operating system. (Drawing includes non-English language text)    Fuel cell stack (100)    Electric heater (110)    Mechanical balance of plant (200)    Fan (280)    Electric power converting section (310)
NOVELTY - This utility model claims one kind of production banaba special base fertilizer's mechanical device, the device belongs to the field of compound fertilizer, comprising a crusher, a fermenting tank, a dryer, a crusher, a mixing machine, wherein the upper machine is provided with dry pig manure inlet's, cow dung inlet's drying, colza cake inlet, corn straw inlet, there is no polluted river mud inlet, mildew feed inlet, and a fermentation tank is provided with a first conveyor upper fermentation tank is provided with an organic fertilizer fermenting agent inlet, a water inlet, a sterilizing deodorant inlet, amino acid I mother liquor inlet, a fermenting tank and drying machine is set between the second conveyor, a drier and a crusher is provided with a third conveyor, crusher is provided with upper inlet of monoammonium phosphate, potassium chloride inlet, humic acid chelated iron inlet, humic acid chelated copper inlet, humic acid chelated calcium inlet, plant-growth regulator inlet, the crusher and mixing machine is provided with a fourth conveyor, upper mixing machine is provided with a finished product outlet.
NOVELTY - A device comprises pre-processing unit (10) in which waste material is screened and crushed, sterilizer (20) in which bacteria and heavy metal wastes are removed, steam regenerator (40), solid-liquid separator (50) in which solid waste is filtered connected to liquid regenerator (60) and solid regenerator (70) in which solid waste is atomized, and remote monitoring system (80).    USE - Device for generation of energy from waste (claimed).    ADVANTAGE - The device produces alternative energy source and prevents garbage incineration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of device for generation of energy from waste. (Drawing includes non-English language text).    Pre-processing unit (10)    Sterilizer (20)    Steam regenerator (40)    Solid-liquid separator (50)    Liquid regenerator (60)    Solid regenerator (70)    Remote monitoring system (80)
NOVELTY - Garbage fertilizer processing system comprises garbage collecting system (10) and fertilizer conversion system (20). Garbage collecting system comprises garbage processing device and garbage transport vehicle, where garbage processing device comprises solid garbage barrels (111) and liquid garbage barrels (112). Fertilizer conversion system comprises solid fertilizer processing system (21) and liquid fertilizer processing system (22).    USE - Garbage fertilizer processing system.    DETAILED DESCRIPTION - Garbage fertilizer processing system comprises garbage collecting system (10) and fertilizer conversion system (20). Garbage collecting system comprises garbage processing device and garbage transport vehicle, where garbage processing device comprises solid garbage barrels (111) and liquid garbage barrels (112). Fertilizer conversion system comprises solid fertilizer processing system (21) and liquid fertilizer processing system (22), where solid processing system comprises multi-stage solid fertilizer packing auger device (211), multi-stage crushing and fermenting device (212) and cross layout packaging device (213). Liquid fertilizer processing system comprises liquid garbage barrel (214), heating and fermenting device (113) and liquid fertilizer packaging device (114).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of garbage fertilizer processing system.    Garbage collecting system (10)    Fertilizer conversion system (20)    Solid fertilizer processing system (21)    Liquid fertilizer processing system (22)    Solid garbage barrels (111)    Liquid garbage barrels (112)    Heating and fermenting device (113)    Liquid fertilizer packaging device (114)    Multi-stage solid fertilizer packing auger device (211)    Multi-stage crushing and fermenting device (212)    Cross layout packaging device (213)    Liquid garbage barrel (214)
NOVELTY - Cultivating material comprises 40-45 pts. wt. cotton seed hull, 25-30 pts. wt. wooden meal, 22-26 pts. wt. bran, 18-22 pts. wt. castor straw, 0.2-0.3 pts. wt. calcium carbonate, 1-1.2 pts. wt. salt, 1-2 pts. wt. sucrose, 7-9 pts. wt. spirulina, 10-11 pts. wt. egg shell powder, 8-9 pts. wt. cucumber seed powder, 12-13 pts. wt. black powder, 4 pts. wt. ginseng flower, 5 pts. wt. Li flowers, 3-4 pts. wt. corn bran, 11-13 pts. wt. corn, 10-12 pts. wt. pork powder, and 3-4 pts. wt. additive.    USE - Cultivating material.    DETAILED DESCRIPTION - Cultivating material comprises 40-45 pts. wt. cotton seed hull, 25-30 pts. wt. wooden meal, 22-26 pts. wt. bran, 18-22 pts. wt. castor straw, 0.2-0.3 pts. wt. calcium carbonate, 1-1.2 pts. wt. salt, 1-2 pts. wt. sucrose, 7-9 pts. wt. spirulina, 10-11 pts. wt. egg shell powder, 8-9 pts. wt. cucumber seed powder, 12-13 pts. wt. black powder, 4 pts. wt. ginseng flower, 5 pts. wt. Li flowers, 3-4 pts. wt. corn bran, 11-13 pts. wt. corn, 10-12 pts. wt. pork powder, and 3-4 pts. wt. additive containing 0.7-0.8 pts. wt. corn, 5-6 pts. wt. Lancea tibetica, 7-8 pts. wt. goose grass, 7-8 pts. wt. yellow wine, 0.2-0.3 pts. wt. coix seed oil, 4-5 pts. wt. corn gluten powder, 0.1-0.2 pts. wt. Vitamin C, 0.1-0.12 pts. wt. manganese sulfate, and 0.08-0.1 pts. wt. ammonium citrate. Additive is prepared by mixing raw materials, standing for 18-20 hours, and mixing to obtain product. An INDEPENDENT CLAIM is included for preparation cultivating material comprising mixing rice, cotton seed hull, wooden meal, and bran mixture for 3-4 hours, adding ginseng flower and 2-3 times water, pulping, adding sucrose, stirring to dissolve, adding remaining raw materials, adding water until water content of 60-65%, and sterilizing at 100 degrees C under normal pressure.
NOVELTY - A paracetamol is prepared by adding acetic acid, p-aminophenol, and zinc metal in reactor, stirring, heating to obtain reaction solution, pumping to dehydration reaction membrane, diffusing until completion, cooling, filtering, crystallizing, and drying.    USE - Preparation of paracetamol for body pain (claimed).    ADVANTAGE - The method improves quality of product, reduces labor intensity, enhances reaction conversion rate, lessens impurity generation, consumes less energy, is highly efficient, and environment-friendly.
NOVELTY - An amorphous darunavir is prepared by dissolving compound in 1st methanol, or methanol-containing mixed solvent to obtain first solution, and dissolving in 2nd methanol, or methanol-containing mixed solvent, precipitating, and separating.    USE - Preparation of amorphous darunavir (claimed).    ADVANTAGE - The obtained compound is highly pure, has good stability,and method is simple, low cost, environment-friendly, and is suitable for industrial production.
NOVELTY - A bio-oil preparing method involves taking appropriate cotton stalk biomass, naturally drying, removing impurity, crushing, and drying to constant weight, and putting in dryer for further use. The processed cotton stalk biomass is added into the reactor, the vacuum is pumped to 10 kPa, after 15-30 minutes, heated at pyrolysis temperature of 400-600 degrees C for 60 minutes, followed by continuously vacuumizing, cooling the pyrolysis steam extracting reactor through the circulating water and ice bath cooling to obtain bio-oil, and non-condensable gases through the gas collected by the collector.    USE - Method for preparing bio-oil by vacuum pyrolysis.    ADVANTAGE - The method enables preparing bio-oil in simple, easy and environmentally friendly manner.
NOVELTY - Recovering a product alcohol from a fermentation broth, comprises: providing a fermentation broth comprising a microorganism, where the microorganism produces product alcohol; contacting the fermentation broth with at least one extractant; and recovering the product alcohol.    USE - The method is useful for recovering a product alcohol from a fermentation broth. The product alcohol is ethanol, propanol, butanol, pentanol, hexanol, or fusel alcohols (all claimed). The product alcohol is useful in industrial and scientific applications such as fuels, reagents and solvents.    ADVANTAGE - The method provides the alcohol with high yield and less toxicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system comprising one or more fermentors comprising an inlet for receiving feedstock slurry and an outlet for discharging fermentation broth comprising product alcohol, and one or more extractors comprising a first inlet for receiving the fermentation broth, a second inlet for receiving extractant, a first outlet for discharging a lean fermentation broth and a second outlet for discharging a rich extractant.
NOVELTY - Method for preparing fermented biological organic fertilizer, involves obtaining cattail as raw material, adding urea and/or duckweed, regulating carbon-nitrogen ratio, and adding fermented bacteria fast rotting agent or beneficial microorganisms (BM) straw rotten agent after fermentation to the mixture. The mass ratio of fermented bacteria fast rotting agent or BM straw rotten agent, urea, duckweed and cattail is 1-40:25-50:650-5000:3000-4000.    USE - The method is useful for preparing fermented biological organic fertilizer which is used in tailings and other mining waste, or complex reclamation of the substrate (all claimed).    ADVANTAGE - The method promotes growth of the plant, and sustainable land resource.
NOVELTY - Preparation of (S)-clopidogrel sulfate or hydrochloride comprises reacting (S)-(+)- alpha -(2-b)thiophene- alpha -(2-methyl acetate) hydrochloride or sulfate (III) and formaldehyde aqueous solution, performing cyclization reaction in the presence of organic solvent, post-processing to obtain (S)-clopidogrel (II); and dissolving in solvent, adding sulfuric acid or hydrochloric acid, carrying out salt-forming reaction, and post-processing. The organic solvent is miscible with water at room temperature.    USE - Method for preparing (S)-clopidogrel sulfate or hydrochloride (claimed).    ADVANTAGE - The method reduces generation of impurities, improves purity and yield, and simplifies purification.    DETAILED DESCRIPTION - Preparation of (S)-clopidogrel sulfate or hydrochloride comprises reacting (S)-(+)- alpha -(2-b)thiophene- alpha -(2-methyl acetate) hydrochloride or sulfate of formula (III) and formaldehyde aqueous solution, performing cyclization reaction in the presence of organic solvent, post-processing to obtain (S)-clopidogrel of formula (II); and dissolving in solvent, adding sulfuric acid or hydrochloric acid, carrying out salt-forming reaction, and post-processing. The organic solvent is miscible with water at room temperature.
NOVELTY - A bio-oil containing lignin and phenol preparation method involves washing the bio-oil with water to obtain an aqueous phase component and a water-insoluble solid and freeze-drying to obtain solid lignin. The solid lignin is dissolved in dioxane and cyclohexane solution, and methanol or ethanol is sequentially added. Ruthenium/HZSM-5 catalyst is mixed with the dissolved solution and hydrogen shifted hydrocracking reaction is performed. The reaction mixture is filtered. The filtrate is evaporated using rotary evaporator under reduced pressure to obtain the finished product.    USE - Method for preparing a bio-oil containing lignin and phenol.    ADVANTAGE - The method enables preparing the bio-oil containing lignin and phenol in a simple and efficient manner with high value-added products and effectively broadening the market prospects of bio-oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for preparing a bio-oil containing lignin and phenol. '(Drawing includes non-English language text)'
NOVELTY - Bio-organic fertilizer comprises microbial agent and organic fertilizer, where the microbial agent includes Japanese beetle Bacillus popilliae, Bacillus subtilis, Bacillus megaterium, Bacillus mucilaginosus, brown spherical nitrogen-fixing bacteria and Bacillus licheniformis and organic fertilizers include livestock and poultry manure mushroom fungus residue.    USE - The bio-organic fertilizer is useful for preventing and treating underground pests (claimed).    ADVANTAGE - The bio-organic fertilizer effectively kills the soil pest larvae in the soil by nitrogen fixation, improves soil structure and crop quality and thus improves organic matter content of the soil and increases crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bio-organic fertilizer, which involves (a) culturing the microbial agent, (b) fermenting the livestock and poultry manure, mushroom fungus residue and bacteria by heating at 60-70 degrees C for 7-10 days, stirring once in every 24 hours, lowering the temperature to 40-60 degrees C and maintaining for 8-10 days to obtain decomposed organic fertilizer and (c) mixing the microbial agent and decomposed organic fertilizer.
NOVELTY - Extracting levodopa from Stizolobium cochinchinensis seed comprises, crushing Stizolobium cochinchinensis seed, extracting (sub-critical) using 1-3% hydrochloric acid, concentrating, allowing to stand overnight to separate out crude extract crystals, dissolving the crude extract with dilute hydrochloric acid, adding activated carbon, refluxing, filtering to remove activated carbon, adjusting pH of filtrate to 3-4 using alkali, allowing to stand overnight for crystallization and drying the crystals.    USE - The method is useful for extracting levodopa from Stizolobium cochinchinensis seed (claimed).    ADVANTAGE - The method is simple, has fewer steps with shortened time, saves reagents and avoids excessive heavy metals which affect the quality of the product.
NOVELTY - A culture material comprises 30-50 wt.% ramie bone, 30-50 wt.% cotton seed hull, 15-25 wt.% bran and 0.05-2.00 wt.% gypsum. It is prepared by drying ramie bone, bagging, sealing, soaking in water for 10-15 hours, drying cotton seed hull and bran, packing, uniformly mixing materials, adding water and stirring until water content is 60-65%.    USE - Culture material and its preparation used for culturing Hericium erinaceus (claimed).    ADVANTAGE - The culture material changes waste into valuable product, reduces environmental pollution and improves economical benefit. The method is simple and convenient.
NOVELTY - A culture material comprises 30-80% ramie hemp, 2-55% cotton seed hull, 15-25% wheat bran and 0.10-2.00% gypsum.    USE - Culture material used for culturing Auricularia polytricha.    ADVANTAGE - The method has reduced environmental pollution and production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of culture material comprising bagging raw materials, sterilizing, adding water to water content of 60-65%, stirring by hand, sealing at 125 degrees C for 2 hours, naturally cooling to room temperature, inoculating, culturing, and spraying insecticide and disinfectant.
NOVELTY - A system has a storing groove, a screw pump, a acidification tank, a mixing tank, a fermentation tank, a heating and temperature controlling device, and feeding and discharging control system.    USE - System is used for fermenting two-stage semi-solid biomass.
NOVELTY - The utility model claims a hydrolyzing device, especially a method for anaerobic hydrolysis treatment technique for printing and dyeing sewage processing process of hydrolyzing device, comprising a grid, a first sedimentation tank, an anaerobic hydrolysis tank and bio-filtering tank and the grid in the biological filter tank is provided with multiple layers of biodegradable. After adopting the said structure, this utility model is a plurality of printing and dyeing sewage. high voltage load hydrolyzing device is greatly improve the processing efficiency of the at the same time reduces the construction investment and operation. At the same time, a biological filter tank, make purifying high load and high efficiency. In addition, with high void ratio, high adhesion area and a water distribution performance of the new plastic a filler cancel the filter pool to a return-flow system, so as to greatly improve the processing efficiency.
NOVELTY - This utility model claims a multi-level baffling composite oxide sewage treatment system for constructed wetland, comprising a water inlet, folded to flow constructed wetland unit, and the water outlet pipe are connected in series to form the feeding area, the current artificial wetland unit and the water outlet section is provided with a group of small basket filler tank, the folded to flow constructed wetland unit is a group of reaction tank connected in series is provided with a step structure, the filling material basket and the bottom flow artificial wetland unit. This utility new type shopping basket easy stuffing change, can be adjusted according to different water quality and a discharge command, a function strengthened filler, solves the problem that the filling saturation and water quality variation, convenient operation and management, using porous water splash plate is uniformly distributed water, a composite oxide and improve the dissolved oxygen in the water, a reaction tank wall of the brick or steel-concrete to replace a basket filler, not to affect microbial and plant has a whole wetland device is between the two stable equilibrium system.
NOVELTY - Removing factory waste water anaerobic fermentation process hydrogen sulfide by introducing less amount air, comprises adding anaerobic fermentation sulfur-containing waste water in a sealed container, where the sulfur-containing waste water comprises hydrogen sulfide containing methane, introducing biogas into the container, subjecting sulfur-containing waste water liquid level spatial aggregation, introducing less amount air, where the introduction volume of air is 7-9%, discharging biogas mixed gas via air outlet pipe into anaerobic fermentation container.    USE - The method is useful for removing factory waste water anaerobic fermentation process hydrogen sulfide by introducing less amount air (claimed).    ADVANTAGE - The method comprises introduction of air without affecting the normal operation condition of anaerobic treatment system; achieves hydrogen sulfide removal rate of more than 99%; does not pollute the environment and is safe for health; avoids the inhibition of methanogenic bacterial activity in anaerobic system; avoids the subsequent desulfurizing process of marsh gas; improves the recovery rate; and reduces the secondary pollution to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for removing factory waste water anaerobic fermentation process hydrogen sulfide by introducing less amount air.
NOVELTY - A sewage is treated by preparing bacteria liquid, mixing bacteria liquid with microbial inoculum in which microbial inoculum contains turfy soil, diatomite and chitosan, low-temperature drying, performing solid-liquid separation, transferring liquid to sedimentation tank, settling, discharging liquid to microorganism reaction tank, adjusting pH of microorganism reaction tank, dosing prepared bacteria liquid and microbial inoculum mixture once daily, continuously dosing for a week, standing for the last 3 days and discharging liquid.    USE - Sewage treatment for garden planning (claimed).    ADVANTAGE - The sewage treatment is environment-friendly, low cost, symbiotic, compatible with different microbial strains, reduces waste by recycling water, purifies garden sewage and removes nitrogen and phosphorus, and has simple preparation.    DETAILED DESCRIPTION - A sewage is treated by mixing 100 pts. wt. Arthrobacter globiformis, 90 pts. wt. Pseudomonas stutzeri, 80 pts. wt. Sphingomonas, 75 pts. wt. Bacillus pumilus, 70 pts. wt. Thiobacillus denitrificans, 50 pts. wt. Phanerochaete chrysosporium, 30 pts. wt. Bacillus licheniformis, and 25 pts. wt. Chryseobacterium to obtain bacteria liquid, mixing bacteria liquid with microbial inoculum with weight ratio of 1:1 in which microbial inoculum contains turfy soil, diatomite and chitosan with mass ratio of 4:2:1, low-temperature drying at 4 degrees C to 6% moisture content, performing solid-liquid separation in which separated solid is used fertilizer, transferring liquid to sedimentation tank, settling for 12 hours, discharging liquid to microorganism reaction tank, adjusting pH of microorganism reaction tank to 7, dosing 10 g/m3 of prepared bacteria liquid and microbial inoculum mixture once daily, continuously dosing for a week, standing for the last 3 days and discharging liquid.
NOVELTY - A Leifsonia shinshuensis (CGMCC NO: 7872), is new.    USE - The L.shinshuensis is useful for degrading decabromodiphenyl diphenyl ether (all claimed).    ADVANTAGE - The L.shinshuensis provides degradation ratio of 90.08%.
NOVELTY - Preparation of biological domestic sewage treatment agent involves mixing bacterial liquid and auxiliary material in weight ratio of 1:1, stirring uniformly, reacting at low temperature of 4-6 degrees C, drying to control water content at 6-8%, and mixing the dried product with carrier comprising sawdust, diatomite and chitosan in mass ratio of 4:2:1. The bacterial liquid contains Bacillus pumilus, B.cereus, Arthrobacter, Pseudomonas stutzeri, Sphingomonas, B.licheniformis and Thiobacillus denitrificans.    USE - The method is useful for preparing biological domestic sewage treatment agent (claimed).    ADVANTAGE - The prepared biological agent that effectively removes all kinds of pollutants in the sewage, as there is symbiotic association between the microorganisms.    DETAILED DESCRIPTION - Method for preparing biological domestic sewage treatment agent involves mixing bacterial liquid and auxiliary material in weight ratio of 1:1, stirring uniformly, reacting at low temperature of 4-6 degrees C, drying to control water content at 6-8%, and mixing the dried product with carrier comprising sawdust, diatomite and chitosan in mass ratio of 4:2:1. The bacterial liquid comprises 20 wt.% Bacillus pumilus, 18 wt.% B.cereus, 16 wt.% Arthrobacter, 12 wt.% Pseudomonas stutzeri, 10 wt.% Sphingomonas, 8 wt.% Thiobacillus denitrificans, 6 wt.% Phanerochaete chrysosporium, 6 wt.% B.licheniformis and 4 wt.% Chryseobacterium.
NOVELTY - Method for improving productivity of 1,3-propylene glycol by fermentation, involves adding activated carbon to crude glycerin obtained as by-product of biodiesel.    USE - The method is useful for improving productivity of 1,3-propylene glycol by fermentation (claimed).    ADVANTAGE - The method does not use organic solvent, consumes less energy and is cost-effective.
NOVELTY - Cured coal comprises 55-60 pts. wt. coal powder, 10-16 pts. wt. potato straw, 35-45 pts. wt. broad bean straw, 1-3 pts. wt. vulcanizing agent, 15-20 pts. wt. blast furnace slag micro powder, 9-16 pts. wt. lime paste, 10-20 pts. wt. slag powder and 3-5 pts. wt. expanded pearl powder.    USE - Used as a cured coal.    ADVANTAGE - The cured coal: is energy-saving and environmentally friendly (claimed), economical and easy to ignite; utilizes renewable source; ensures complete combustion; has high heat efficiency; solves the problem of short fuel combustion period of pure straw; reduces sulfur and dust emissions; and is suitable for use in industries, flue-cured tobacco, biomass generation and in residents.
NOVELTY - The reformer has an oxygen supply path which supplies oxygen (14) from an oxygen production apparatus (13) to the upper space (4). The char generated because the volatile matter of solid carbon (11) from the solid carbon supply apparatus (10) burns by supplying oxygen from the oxygen production apparatus. Gasification of a char (22) is performed while a char is adsorbed. The tar makes this char a catalyst and modification of a tar is performed when gasifying gas distributes the char fixed bed (23) maintained by setting modification temperature.    USE - Char fixed bed reformer for gasification system which heats and gasifies biological raw materials. Uses include but are not limited to coal, petroleum refining residues, wood chips, and sludge.    ADVANTAGE - Modification of a tar can be performed while manufacturing a char with the supply of solid carbon, The outstanding effect that the apparatus for char manufacture is omissible from this can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view which shows the outline of the char fixed bed reformer and a reformer top view. (Drawing includes non-English language text).    Upper space (4)    Solid carbon supply apparatus (10)    Solid carbon (11)    Oxygen production apparatus (13)    Oxygen (14)    Char (22)    Char fixed bed (23)
NOVELTY - Neutralizing cationic soil comprises inserting 20 cm rod-like organic fertilizer comprising cation exchange resin, sainfoin, crown vetch, cow dung, crushed straw, phosphorus and potassium bacteria, polyvinyl alcohol, and fermentative bacteria into saline alkali soil ridge side, and exposing 1-2 cm of fertilizer above the soil; adding corn starch, to water, heating to 70-75 degrees C for 1 hour, cooling to 45 degrees C to obtain paste, and spraying on surface of soil to obtain thin film; and inserting fertilizer to other side of ridge every 20-25 days, rotating, and spraying with paste.    USE - Method for neutralizing cationic soil (claimed).    ADVANTAGE - The method is simple and easy to use, has simple product ratio, reduces salt content of soil, increases soil microbial and enzyme activities, and promotes growth of plant roots.
NOVELTY - Desulfurization agent comprises 90-95 wt.% of steel slag, 4.9-9.5 wt.% of active iron component, and 0.1-0.5 wt.% of oxalic acid.    USE - The desulfurization agent useful in anaerobic digestion of sludge such as domestic sewage (claimed).    ADVANTAGE - The desulfurization agent has simple preparation, high reliability, can effectively reduce the sulfur content in the gas, thus improving energy utilization of the biogas.    DETAILED DESCRIPTION - An INDEPENDANT CLAIM is included for preparing the desulfurization agent comprising crushing and sieving the steel slag to obtain steel slag micro powder, adding the obtained steel slag micro powder with active iron component and oxalic acid, uniformly mixing, and grinding using a 200 meshes sieve.
NOVELTY - Preparation of a liquefied methane comprises introducing 25-30 MPa air and synthetic ammonia at 6-12 MPa to an ammonia recycling system, adding ammonia gas in a gas-liquid separator through a heater at 30 degrees C, water washing at 40-55 degrees C, introducing to a membrane separation system, and introducing to a molecular sieve adsorption system; cooling the mixture to - 137 to - 140 degrees C, introducing to a gas-liquid separator, decompressing, introducing to a rectifying tower and methane rectifying tower, introducing to a distillation column, and discharging argon gas; and reheating the gas at 20-25 degrees C.    USE - Method for the preparation of a liquefied methane (claimed).    ADVANTAGE - The method reduces environmental pollution.    DETAILED DESCRIPTION - Preparation of a liquefied methane comprises:    (A) introducing 25-30 MPa air and synthetic ammonia at 6-12 MPa to an ammonia recycling system, recycling ammonia with the air mixing pressure in a high pressure water washing tower, removing residual ammonia gas, adding ammonia gas in a gas-liquid separator through a heater at 30 degrees C, water washing at 40-55 degrees C, where the ammonia content is less than 50 ppm, introducing to a membrane separation system, extracting hydrogen at 1.5-1.8 MPa, and introducing to a molecular sieve adsorption system to remove water and obtain a moisture content of less than less than or equal to 1 ppm;    (B) cooling the mixture to - 137 to - 140 degrees C, introducing to a gas-liquid separator, further cooling at - 148 degrees C, decompressing, cooling to - 159 degrees C to - 162 degrees C, introducing to a rectifying tower and methane rectifying tower, introducing to a distillation column, discharging argon gas, and recycling the cold gas to the heat exchanger; and    (C) reheating the gas at 20-25 degrees C, and introducing to the molecular sieve adsorption system at 180-210 degrees C as regenerated gas.
NOVELTY - A furnace liquid fuel comprises 50-80 pts. wt. alcohol mixture, 5-10 pts. wt. gasoline, 2-5 pts. wt. combustion improver, 2-5 pts. wt. surface active agent, 0.1-0.5 pts. wt. antiknock agent, 0-0.05 pts. wt. smoke suppressor, 1-3 pts. wt. odor removing agent, 1-3 pts. wt. antioxidant, and 0-20 pts. wt. toluene.    USE - Furnace liquid fuel.    ADVANTAGE - The liquid fuel has calorific value of 8500-12500 kJ/kg, and can improve resource utilization rate and pollution to the environment.
NOVELTY - Hydrothermal carbonization of solid fuel comprises adding bio-oil water phase component in the high pressure reaction kettle, tightly covering under the protection of nitrogen, hydrogen or inert gas, increasing temperature, stirring, hydrothermally carbonizing at 100-300 degrees C for 2 hours, filtering, separating, and drying to obtain solid fuel.    USE - Method of hydrothermal carbonization of solid fuel (claimed).
NOVELTY - A cathode furnace garbage fuel comprises a wood garbage block and flame-retardant particles. The total volume of flame-retardant particles is 8-15 volume% of total volume of wood garbage block. The flame-retardant particles are dispersed on the outer surface of garbage block and a flame barrier layer is formed when block is burned. The distribution area of flame retardant particles on the outer surface of block is 70-85% of external surface area of block.    USE - Cathode furnace garbage fuel (claimed).    ADVANTAGE - The cathode furnace garbage fuel is stably, safely, easily and efficiently manufactured.
NOVELTY - A biodiesel is prepared from sludge palm oil by preheating sludge palm oil, acidifying, evaporating at less than or equal to 200 degrees C, adding catalyst, performing catalytic hydrocracking to obtain short-chain fatty acids, alkene and alkane compounds, pre-esterifying at 70-75 degrees C, mixing 98 vol.% methanol and 3 wt.% concentrated sulfuric acid, reacting for 0.5 hour to obtain fatty acid alkyl esters, discharging acidic water, standing for 15 minutes, dehydrating oil, distilling at 360 degrees C, esterifying to obtain biodiesel, and refining using biodiesel oil refining device.    USE - Method for preparing biodiesel from sludge palm oil (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of catalyst comprising pulverizing nickel salt, granulating to spherical or cylindrical granules with diameter of 0.5-4.0 mm and pore diameter of 200-300 nm, and sintering at 800 degrees C; and    (2) biodiesel oil refining device comprising catalytic cracking device, pre-esterification reaction device, rectifying device, boiler, water processing system, heating tank, catalytic cracking tower, cooler, recovering tank, heat exchanger, raw oil pre-heating tank, high temperature oil pump, pre-esterification reaction tank, methanol tank, acidic water washing tank and sulfuric acid tank.
NOVELTY - Obtaining liquid fuels from carbonaceous polymeric materials involves combining processes and thermal catalytic cracking by a sequence of unit operations, ensuring maximum efficiency, combining with catalysts and additives for the production of liquid fuels.    USE - The process is useful for obtaining liquid fuels from carbonaceous polymeric materials (claimed).    ADVANTAGE - The method minimizes the production of unprocessed solid, maximizes the production of liquid hydrocarbons by the addition of 0.5-2% of red clay, and improves the process yield by adding a proportion of 1-5% of sodium bentonite and calcium. The method uses a mixture of catalysts and additives which does not require chlorine and which is an improvement of the corrosion process at the environmental level (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a mixture of catalysts and additives which allows to decrease the energy (temperature) required for the cracking reaction on the order of 100-170 degrees C; a mixture of catalysts and additives with aluminosilicate zeolites formed by such porous structure with pore diameters between 3 and 30 Angstroms, alumina, kaolin, clays rich in iron oxides, derivatives of carboxylic or polycarboxylic acids, calcium and sodium bentonites and silicates to generate stable liquid fuels through a sequence of unit operations; a mixture that uses aluminosilicate zeolites type of porous structure with pore diameters of 3 to 30 Angstroms along with adjuvants additives derived from carboxylic acids and polycarboxylic to ensure the absence of oxygen gas (O2) in proportion of 2% in the case of plastics up to 10% in the case of biomass; or a cracking catalyst mixture used as an additive to clay rich in iron oxides which promotes the hydrogenation reaction in the core.
NOVELTY - The method involves semi-hardening the thermosetting seal to such an extent that adhesion between the thermosetting sealing material (150) and a pair of separator plate (130,140) is not stripped, when the pressurization is released. The between of pair of separator plates are heated at temperature lower than temperature at time of hot press, without pressurizing, and further hardening thermosetting seal.    USE - Manufacturing method for fuel cell.    ADVANTAGE - The manufacturing method suppress disappearance of the elasticity of the gas diffusion layer by the hot press at the time of single cell manufacture, and suppress change of the shape of the gas diffusion layer at the time of hot press. The occupancy time of a hot press machine can be decreased and productivity can be improved, since the thermosetting seal is divided into the further hardened heating process.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the joining method of the separator plate of 2 sheets to the membrane-electrode gas diffusion layer conjugate. (Drawing includes non-English language text).    Membrane electrode assembly (100)    First gas diffusion layer (110)    Second gas diffusion layer (120)    Separator plates (130,140)    Thermosetting sealing material (150)
NOVELTY - Product comprises a mixture of acetal of hydroxymethyl furaldehyde, levulinic ester and alkoxy benzenes. The product is obtained by e.g.: dissolving sugar cane or similar crop containing e.g. cellulose in mixture of N-alkyl imidazolium chloride (NAIC), 37% hydrochloric acid and alcohol; hydrolyzing cellulose into acetal of glucose; hydrolyzing lignin in phenolic compounds; evaporating alcohol and water; dehydrating glucose acetal to acetal of hydroxymethyl furfural; and adding to reaction mixture an alcohol to get acetal of hydroxymethyl furfural, ester of levulinic acid and alkoxy benzenes.    USE - The product is useful as a biofuel which is useful for combining with both gasoline and diesel oil for motor cars (claimed).    DETAILED DESCRIPTION - Product comprises a mixture of acetal of hydroxymethyl furaldehyde, levulinic ester and alkoxy benzenes. The product is obtained by: dissolving sugar cane or a similar crop containing cellulose, hemicellulose, sugar and lignin in a mixture of N-alkyl imidazolium chloride (NAIC), 37% hydrochloric acid and alcohol; hydrolyzing cellulose into the acetal of glucose; hydrolyzing the lignin in phenolic compounds; evaporating the alcohol and water; dehydrating the glucose acetal to the acetal of hydroxymethyl furfural; adding to the reaction mixture an alcohol to produce the acetal of hydroxymethyl furfural, the ester of levulinic acid and the alkoxy benzenes; extracting the reaction products from the ionic liquid phase; taking out the residues of the ionic liquid from the organic phase by extracting the ketone extract with water; and evaporating the ketone extract to isolate the reaction products.
NOVELTY - Fuel object comprises: 60-80 wt.% of a particulate derived from corn stover having a particle size of 100-35000 mu ; 20-40 wt.% of a wood fiber having a particle size of 100-30000 mu ; and 1-10 wt.% of sodium bicarbonate. The fuel object has: a maximum dimension of 6 cm; and a volume of 10-100 cm3.    USE - The fuel object is useful: in a fuel source; for reducing emissions upon combustion of a conventional fossil fuel which includes coal products or petroleum products, where the coal products are bituminous coal, anthracite coal or peat, the coal comprises eastern coal, and hydrochloric acid, sulfur dioxide and nitrogen oxides are reduced (all claimed); and in power generation technologies including stoker, fluidized bed, gasifier, cyclonic, direct-fired, and pulverized coal technologies.    ADVANTAGE - The fuel object: has a reduced moisture content of less than 14 wt.%; is substantially free of coal as a heat source; provides high heat out put (at least 7000 BTU/lb (3500 cal/g)); significantly reduces air emissions (including sulfur dioxide, nitrogen oxides, hydrochloric acid, carbon monoxide, carbon dioxide, and mercury) compared to coal with no loss of boiler or furnace efficiency; is readily made in a cost effective manner; can be transported and handled at low cost; is mechanically stable; and can be used in existing solid fuel systems with little or no modifications.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a fuel source comprising the fuel object and a conventional fossil fuel; and    (2) reducing emissions upon combustion of a conventional fossil fuel, comprising co-firing the fuel object with a conventional fossil fuel.
NOVELTY - Producing pure hydrogen comprises passing a synthesis gas through an upstream of a presses swing adsorption (PSA) purification unit (1008) into an exchanger (1006) for complete condensation of the water contained in the gas discharged from an autothermal reforming reactor (ATR), where the exchanger comprises a first portion which performs cooling of the synthesis gas using a cold fluid to the desulfurized load, and a second portion that continues cooling to total condensation of the water contained in the synthesis gas to 15-40 degrees C using cooling water cooled by a cooling tower.    USE - The method is useful for producing pure hydrogen from a hydrocarbon load or ethanol containing sulfur products (claimed), where the hydrocarbon load is taken from gasoline and the ethanol is output from a biomass.    ADVANTAGE - The exchanger located in the upstream of the PSA, thus ensuring the total condensation of water in output, and avoiding discontinuity in the flow of synthesis gas. The method is capable of producing pure hydrogen in a simple manner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view illustrating a method for producing hydrogen.    Vaporized load-water pipe (105)    Desulfurization reactor (1001)    Heat exchanger (1006)    Balloon (1007)    PSA purification unit. (1008)
NOVELTY - Fuel comprises biomass waste and paper pulp that are shaped and dried to form the fuel behaving like a coal.    USE - The fuel is useful in a wood or coal based heating apparatus.
NOVELTY - A single component, granular, bifunctional composite for removal of inorganic nitrogen and phosphorus from an aqueous environment comprises a zeolite coupled to ferric ion through cation exchange.    USE - For removal of inorganic nitrogen and phosphorus from an aqueous environment and converting these into continuous release fertilizer which is used for fertilize a field (claimed).    ADVANTAGE - The single component, bifunctional granular composite can continuous slow release nitrogen and/or phosphorus to produce nitrogen and phosphate fertilizer in situ resulting in less eutrophication and contamination of groundwater. The single component, bifunctional granular composite uses more waste materials on the fields thereby increasing the increasing herd capacity on a dairy farm. The single component, bifunctional granular composite is easy to use; is environmentally friendly and non-polluting, and totally nontoxic for all animal and plant life, including microscopic and microbial species found in soil. The composite is sustainable as they return to the earth through recycling in unaltered form. The composite addresses both the phosphate and ammonia issues simultaneously either independently or concurrently.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) to remove inorganic nitrogen and phosphorus from an aqueous environment involving contacting the environment with the composite; and    (2) a solid precipitate obtained by the method (M1).
NOVELTY - The device has an input unit inputting operation information of a vehicle, where the operation information is separated according to frequency band of a sine wave. An audio generating unit generates engine noise according to the frequency band of the sine wave. An output unit outputs the engine noise generated by the audio generating unit. A storage unit stores cylinder number information and engine type information of the vehicle. A control unit controls the audio generating unit. An amplifier amplifies the engine noise generated in the audio generating unit to a fixed level.    USE - Engine sound generation device for a fuel cell vehicle (claimed).    ADVANTAGE - The device generates the engine noise of the vehicle in an effective manner, thus improving safety of a pedestrian. The device determines change of speed of the vehicle according to movement of the vehicle, thus enhancing auditive contentment of an operator.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a fuel cell vehicle    (2) an engine noise generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an engine sound generation device. '(Drawing includes non-English language text)'
NOVELTY - Reforming process comprises: contacting naphtha boiling range feedstock in penultimate stage of multistage reforming process at first reforming pressure with first reforming catalyst to produce penultimate effluent (11); contacting at least portion of penultimate effluent in final stage of multistage reforming process at second reforming pressure with second reforming catalyst; regenerating final stage catalyst while reforming is taking place in penultimate stage; and temporarily increasing severity of penultimate stage to meet research octane number target for product reformate.    USE - The reforming process is useful for producing product reformate/high octane product, where the reformate is used as a fuel or as a blend stock for a fuel.    ADVANTAGE - The reforming process provides high octane products at high liquid yield and improved hydrogen production.    DETAILED DESCRIPTION - Reforming process comprises: contacting a naphtha boiling range feedstock in a penultimate stage of a multistage reforming process at a first reforming pressure with a first reforming catalyst to produce a penultimate effluent (11); contacting at least a portion of the penultimate effluent in a final stage of the multistage reforming process at a second reforming pressure with a second reforming catalyst to produce a final effluent comprising a final reformate, where the final reformate has a target research octane number that is higher than an intermediate reformate (25); regenerating the final stage catalyst while reforming is taking place in the penultimate stage; and temporarily increasing the severity of the penultimate stage to meet the research octane number target for the product reformate while the final stage catalyst is being regenerated.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the reforming process.    Penultimate effluent (11)    Light reformate (23)    Intermediate reformate (25)    Heavy reformate (26)    Separation zone (40)
NOVELTY - Production of synthetic fuels from biolipid sources involves treating a biomass with a culture of hyperthermophillic organisms to provide a biomass culture; culturing the biomass culture under conditions such that hydrogen gas is produced; and utilizing the hydrogen gas.    USE - For the production of synthetic fuels, for forming straight chain paraffins or synthetic parafinnic kerosene which is used for producing fuel (claimed).    ADVANTAGE - The present method utilizes hyperthermophilic organisms that are capable of growing on biomass that has been previously fermented by methanogenic microorganisms, to produce heat or electricity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) straight chain paraffins or synthetic parafinnic kerosene produced by the method (m1);    (2) fuel, produced by formulating fuel with the synthetic paraffinic kerosene
NOVELTY - The system has a gear connected to a motor according to operation of the motor. A direct driving apparatus drives the motor through a belt. The motor is operated based on DC voltage, which is generated by a fuel cell portion according to status of charge (SOC) of a secondary battery. A start switch drives an external load. A speed controller controls rotating speed of the motor according to a command of the fuel cell portion. The fuel cell portion supplies DC voltage to the secondary battery. A stack generates DC voltage reacting oxygen among methanol fuel and air.    USE - Motor direct driving system.    ADVANTAGE - The fuel cell portion is directly connected to the motor, so that output voltage generated from the fuel cell portion is supplied to the motor, thus reducing smoke, vibration and noise generation. The apparatus avoids requirement of an additional secondary battery so as to reduce manufacturing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a motor direct driving system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a motor direct driving system. '(Drawing includes non-English language text)'
NOVELTY - Biofertilizer comprises at least one bacterial strain comprising Pseudomonas aeruginosa strain AGKT1, Serratia marcescens strain AGKT4 and Bacillus amyloliquefaciens.    USE - The biofertilizer is useful in the agriculture for crop and soil improvement, as biofungicide or as plant growth regulator. Tests details are described but no results given.    ADVANTAGE - The bacteria isolates are capable of solubilizing phosphorus in a liquid medium at an amount of at least 100 mu g/ml, thus providing optimized biofertilizer with high crop growth and yield.
NOVELTY - The detector has a diverging light emitter (AB) directed toward a first coaxial parabolic cap (1-1). A light receiver (CD) is directed toward a second coaxial parabolic cap (1-2). The caps are distant by sum of focal distances plus thickness (d) of a wafer (11). The wafer is formed of portions of plates of material transparent to wavelength to be detected. The plates are placed against each other with an interposed layer of opaque material i.e. metal, pierced with an opening providing direct optical communication between the light emitter and the light receiver.    USE - Optical absorption gas detector for detecting gas in atmosphere. Uses include but are not limited to carbon dioxide, carbon monoxide, methane and toxic gas e.g. xylene or toluene, released by paint.    ADVANTAGE - The detector is simple to manufacture and tolerant to misalignments among an emitter, reflective surfaces and a receiver. The detector performs metal deposition to make inner surfaces of hemispherical cap reflective to be performed, so that the reflective surface is slightly rough to blur an image of filament on the receiver. The detector provides large positioning tolerance due to fact that an emitting portion and a receiving portion of an emitter-receiver assembly are assembled head-to-tail in a single block, so that the emitter and the receiver displace together, thus compensating for consequences of possible mispositionings.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of an optical gas detector tolerant to misalignments.    Diverging light emitter (AB)    Light receiver (CD)    Thickness of wafer (d)    Coaxial parabolic caps (1-1, 1-2)    Focal plane (5)    Wafer (11)
NOVELTY - The method involves outputting first recycling product (131) and first gas-phase component (132). First gas phase ingredient is received, and small molecular substance is removed. Second heat exchanger is provided with first flow channel for receiving second gas phase ingredient (142) to second gas-liquid separating device. Third flow passage is provided for receiving liquid phase component from second gas-liquid separating device. Fourth flow passage is provided for receiving output and gas phase component of first gas expansion device.    USE - Method for recovering exhaust gas for production of olefin polymer.    ADVANTAGE - The energy consumption of system can be reduced. The manufacturing cost of the system can be reduced. The small molecular substance can be separated, so that the recovery rate of hydrocarbons can be improved. The de-volatilization can be achieved for recycling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for recovering exhaust gas for production of olefin polymer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for recovering exhaust gas for production of olefin polymer.    Gas compression device (120)    Gas-liquid separating device (130)    Recovery component (131)    Gas-phase component (132)    Gas phase ingredient (142)
NOVELTY - Producing organic fertilizer in rice seedling method comprises mixing 2% of crop straw and manioc waste having a ratio of 1:1, composting, fermenting, polishing using a polishing machine, mixing, adding water retention agent, root promoting powder and adhesive, uniformly mixing, stacking half month in a stacking process, polishing, sieving and crushing, extracting indoor monitoring sample, and packaging using a bag.    USE - The method is useful for producing organic fertilizer, which is useful for rice seedling (claimed).    ADVANTAGE - The method produces the organic fertilizer with high quality, nutrient content and reduced environment pollution in large scale manner.
NOVELTY - The biomass microwave hot coke releasing device has microwave cracking furnace (1) which is connected to cyclone separator (2), condensing system (3) and alkali washing tank (5). The air outlet of cyclone separator is connected to microwave cracking furnace and condensing system. Discharge hole of cyclone separator is connected with tar and particulate matter. The condensing system is connected to oil tank (33). The air outlet of condensing system is connected with alkali washing tank. The air outlet of alkali washing tank is connected with gas pipeline.    USE - Biomass microwave hot coke releasing device.    ADVANTAGE - The ratio of the bio-oil can be improved. The raw material is not required with fine crush, so that usage of large-scale of biomass can be reduced. The cost of the hot coke releasing device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biomass microwave hot coke releasing device.    Microwave cracking furnace (1)    Cyclone separator (2)    Condensing system (3)    Alkali washing tank (5)    Oil tank (33)
NOVELTY - Carbonized yellow hollyhock is prepared by drying yellow hollyhock so that amount of water in yellow hollyhock is reduced to 2-12%, crushing into particles with diameter of 0.1-8 mm, extruding at 150-350 degrees C, placing in carbonization furnace and carbonizing at 300-800 degrees C for 36-48 hours, preserving for 24-48 hours, and obtaining finished product.    USE - Preparation of carbonized yellow hollyhock (claimed).    ADVANTAGE - Carbonized yellow hollyhock can be prepared at low cost, and wastes and environmental pollution can be reduced.
NOVELTY - Biodiesel oil preparation involves refluxing sodium hydroxide (catalyst), choline chloride (eutectic solvent) and vegetable oil or fatty acid ester of glycerol in methanol solvent with heating for 2-6 hours to obtain reaction mixture. The obtained reaction mixture is cooled at room temperature to form a liquid-liquid biphasic system, where upper layer is crude product, and lower layer is a eutectic mixture. The obtained crude product is separated, washed and then dried to obtain biodiesel oil product.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method enables to produce pure biodiesel oil that is cost effective, eco-friendly and easy to recycle, where emulsification is not performed due to presence of eutectic mixture.    DETAILED DESCRIPTION - Biodiesel oil preparation involves refluxing sodium hydroxide (catalyst), choline chloride (eutectic solvent) and vegetable oil or fatty acid ester of glycerol (I) in methanol solvent with heating for 2-6 hours to obtain reaction mixture. The obtained reaction mixture is cooled at room temperature to form a liquid-liquid biphasic system, where upper layer is crude product, and lower layer is a eutectic mixture. The obtained crude product is separated, washed and then dried to obtain biodiesel oil product (II). Lower layer of the eutectic mixture contains un-reacted raw materials i.e. catalyst and glycerol are recycled.    R=carbon chain fatty acids.
NOVELTY - Treating pellets, preferably wood pellets, comprises introducing the pellets into a gas stream to discharge fines, and partially ionizing the gas stream and/or the pellets by an ionizing device (4).    USE - The method is useful for treating pellets, preferably wood pellets (claimed).    ADVANTAGE - The method allows the effective treatment of wood pellets in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for the treatment of pellets, preferably wood pellets, comprising an air separator (7), in which the pellets are introduced into the gas stream for discharging fine particles, and the ionizing device by which the gas stream and/or the pellets are at least partially ionized.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic sectional view of a device for the treatment of pellets.    Ionizing device (4)    Riser pipe (5)    Air separator (7)    Supply channel (8)    Flap. (10)
NOVELTY - A biomass is pulverized to obtain biomass ground material. An iron content-containing material is pulverized to obtain iron content containing-ground material. The biomass ground material and iron content containing-ground material are mixed, to obtain mixture. The mixture is dry-distilled in rotary kiln, and dry-distilled material is mixed with mixture of biomass charcoal and carbon deposited-iron content-containing material. The biomass is dry-distilled to obtain biomass charcoal, which is used for iron-making process.    USE - Utilization of biomass for iron-making process.    ADVANTAGE - The method enables utilization of biomass with high yield. The iron-making process is carried out efficiently using biomass.    DETAILED DESCRIPTION - A biomass is pulverized to obtain biomass ground material. An iron content-containing material is pulverized to obtain iron content containing-ground material. The biomass ground material and iron content containing-ground material are mixed, to obtain mixture. The mixture is dry-distilled in rotary kiln, and dry-distilled material is mixed with mixture of biomass charcoal and carbon deposited-iron content-containing material. The biomass is dry-distilled to obtain biomass charcoal, which is used for iron-making process. The ratio of average-particle diameter of biomass ground material to average-particle diameter of iron content containing-ground material is 5 or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining the utilization method of biomass. (Drawing includes non-English language text)    Biomass (1)    Iron content-containing material (2)    Mixing process (5)    Dry distillation process (6)    Generated gas (7)
NOVELTY - Method for preparing substance which has adsorptivity with respect to saccharide excessive degradation product or lignin degradation product involves heat-processing saccharified residue of the plant biomass containing lignin in oxygen environment.    USE - The method is useful for preparing substance which is used as adsorption agent with respect to saccharide excessive degradation product or lignin degradation product (claimed).    ADVANTAGE - The method enables to prepare product which has excellent adsorptivity, and is cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the water-insoluble material involves saccharification pre-processing on the plant biomass containing lignin, and performing enzyme saccharification process on the pre-processed raw material;    (2) substance which has adsorptivity with respect to saccharide excessive degradation product or lignin degradation product is obtained by performing the above-mentioned method;    (3) adsorption agent comprising the above-mentioned substance; and    (4) method for preparing the fermented material of saccharide involves performing saccharification pre-processing on the plant biomass containing lignin, performing enzyme saccharification process on saccharification pre-processed material, performing fermentation on the saccharification pre-processed material, performing fermentation on the enzyme saccharification processed raw material, and contacting the obtained product with the above-mentioned substance.
NOVELTY - Converting a biomaterial to a fuel product, comprises: providing a biomaterial comprising coal, cellulosic products, animal parts, animal fat, vegetable oil and/or food grains; hydrolyzing the biomaterial using a base or alkalized catalyst comprising hydrides of groups IA, IIA or IIIA metals, oxides or hydrides of groups IA or IIA metals, or groups of organometallic compounds containing groups IA, IIA or IIIA, at a temperature of 319 degrees C to yield a reaction product; and acidifying the reaction product to form carbon dioxide and a liquid hydrocarbon fuel product.    USE - The method is useful for converting a biomaterial to a fuel product such as a liquid hydrocarbon fuel product i.e. a distillable product that can be processed by a petroleum refinery (all claimed).    ADVANTAGE - The one-step method easily converts biomaterial to the fuel product with high yield along with the recovery of high purity carbon dioxide product, even under mild operation conditions without the need for recycling of unconverted feeds.    DETAILED DESCRIPTION - Converting a biomaterial to a fuel product, comprises: providing a biomaterial comprising coal, cellulosic products, animal parts, animal fat, vegetable oil and/or food grains; hydrolyzing the biomaterial using a base or alkalized catalyst comprising hydrides of groups IA, IIA or IIIA metals, oxides or hydrides of groups IA or IIA metals, or groups of organometallic compounds containing groups IA, IIA or IIIA, at a temperature of 319 degrees C to yield a reaction product, where a hydrocarbon fuel product in the reaction product has a hydrogen to carbon ratio of 1.6; and acidifying the reaction product to form carbon dioxide and a liquid hydrocarbon fuel product.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of a method for converting biomaterial to fuel product.
NOVELTY - An oxygen-permeating membrane (10) permeates oxygen from a high-oxygen pressure side to a low-oxygen pressure side by making an oxygen-partial-pressure difference into a driving force, and comprises a mixture of stabilized zirconia as oxygen ion conductor and strontium-based composite oxide (I) as electronic conductor.    USE - Oxygen-permeating membrane is used for extracting oxygen for producing hydrogen used in fuel cell.    ADVANTAGE - The oxygen-permeating membrane has excellent stability.    DETAILED DESCRIPTION - An oxygen-permeating membrane permeates oxygen from a high-oxygen pressure side to a low-oxygen pressure side by making an oxygen-partial-pressure difference into a driving force, and comprises a mixture of stabilized zirconia as oxygen ion conductor and strontium-based composite oxide of formula: Sr1-xMxTi1-yM'yO3- (I) as electronic conductor.    M=element chosen from rare-earth elements;    M'=element chosen from niobium or tantalum;    x,y=0-0.3;and    z=0-0.2.    N.B. z is defined in the disclosure, but not in the claims.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional schematic view of the oxygen-permeating membrane.    Oxygen-permeating membrane (10)    Reforming raw material flow path (16)    Air flow path (18)    Modifier (20)
NOVELTY - Isolated Clavispora spp.,, which is deposited with the United States Department of Agriculture, and Agricultural Research Patent Culture Collection as accession deposit number Northern Regional Research Laboratory (NRRL) Y-50464, is new.    USE - The isolated Clavispora spp. is useful for producing ethanol from the fermentation of cellulosic material including a lignocellulosic biomass such as agricultural residues, wood, municipal solid wastes, paper and pulp industry wastes, herbaceous crops, and xylose-extracted corncob residue (all claimed).    ADVANTAGE - The isolated Clavispora spp. economically and efficiently produces the ethanol with high yield and reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing ethanol from the fermentation of cellulosic material comprising fermenting the yeast strain with cellulosic material under conditions for a period of time sufficient to allow fermentation of at least a portion of cellulosic material to ethanol.
NOVELTY - Briquettes of coal contains coal dust comprising brown coal having low to moderate calories, bituminous and/or sub-bituminous, biomass powder, molasses obtained from manufacture of crystal sugar residues, salt form of potassium nitrate and/or sodium nitrate, cleaners containing alkali metal comprising calcium oxide, calcium hydroxide or calcium carbonate and other salts containing silicon aluminate and iron salts, and components made adhesive jelly from tapioca flour.    USE - Briquettes of coal is used for furnace or stove for counterflow combustion, and household cooking.    ADVANTAGE - The environmentally-friendly briquettes of coal having excellent burning property and non-adhesive property, is manufactured economically.    DETAILED DESCRIPTION - Briquettes of coal comprises coal dust comprising brown coal having low to moderate calories, bituminous and/or sub-bituminous, biomass powder, molasses obtained from manufacture of crystal sugar residues, long-chain hydrocarbon molecules having more than 16 carbon atoms obtained from olive oil, black diesel oil or fuel oil, salt form of potassium nitrate and/or sodium nitrate, cleaners containing alkali metal comprising calcium oxide, calcium hydroxide or calcium carbonate and other salts containing silicon aluminate and iron salts, and components made adhesive jelly from tapioca flour.
NOVELTY - A pitavastatin calcium is prepared by mixing organic solvent, 2-cyclopropyl propyl-3-(diethoxyphosphinyl)-4-(4-fluorophenyl)quinoline, (3R, 5S)-7-(2-cyclopropyl-4-(4-fluorophenyl)-3-quinolinyl)-3,5-di-3,5-dihydroxy-6-oxo-3,5-o-isopropylidine-hexanoic acid tert.-butyl ester, and tert. butyl lithium at - 90-0 degrees C to obtain (3R, 5S, 6E)-7-(2-cyclopropyl-4-(4-fluorophenyl)-quinolin-3-yl)-3,5-dihydroxy-3,5-o-isopropylidene-6-heptonic acid tert.-butyl ester, and adding de-protecting agent hydroxylamine hydrochloride under to alcohol/ketone/water mixed solution at 20-100 degrees C.    USE - Preparation of pitavastatin calcium (claimed).    ADVANTAGE - Preparation process increases yield, reduces reaction step, has mild reaction condition, and is earth-frienldy.    DETAILED DESCRIPTION - A pitavastatin calcium of formula (VII) is prepared by mixing organic solvent, 2-cyclopropyl propyl-3-(diethoxyphosphinyl)-4-(4-fluorophenyl)quinoline of formula (III), (3R, 5S)-7-(2-cyclopropyl-4-(4-fluorophenyl)-3-quinolinyl)-3,5-di-3,5-dihydroxy-6-oxo-3,5-o-isopropylidine-hexanoic acid tert.-butyl ester of formula (IV), and tertiary butyl lithium at - 90-0 degrees C to obtain (3R, 5S, 6E)-7-(2-cyclopropyl-4-(4-fluorophenyl)-quinolin-3-yl)-3,5-dihydroxy-3,5-o-isopropylidene-6-heptonic acid tert.-butyl ester of formula (V), adding de-protecting agent hydroxylamine hydrochloride under to alcohol/ketone/water mixed solution at 20-100 degrees C to obtain (3R, 5S, 6E)-6-(2-cyclopropyl-4-(4-fluorophenyl)-quinolin-3-yl-vinyl)-4-dihydroxy-3,4,5,6-tetrahydro-2H-pyran-2-one of formula (VI), performing alkaline hydrolysis reaction, and performing salt forming reaction. .
NOVELTY - Processing food residue comprises placing food debris in an airtight stainless steel container; sealing, and fermenting; and removing food residue.    USE - Method for the processing food residue (claimed).    ADVANTAGE - The method is simple and convenient, is sanitary, and environment-friendly.
NOVELTY - The engine system (100) comprises a spark-ignited internal combustion engine (110) powered by a gaseous fuel, an air intake providing communication with the internal combustion engine, and an exhaust system (120) set in communication with the internal combustion engine. The exhaust system comprises a methane oxidation catalyst through which at least a portion of the exhaust gas flows, and an exhaust gas recirculation line set in communication with the air intake. The recirculation line is positioned upstream of methane oxidation catalyst and downstream of a turbine (160).    USE - Internal combustion engine system of internal combustion engine such as spark-ignited gaseous fuel internal combustion engine.    ADVANTAGE - An exhaust system for gaseous-powered engine that has an after-treatment catalyst such as a three-way catalyst capable of methane oxidation and exhaust gas recirculation strategies, is provided. The combustion temperatures are reduced and brake thermal efficiency is increased, so that the load carrying ability and power density of the engine are improved. The amount of nitrogen oxides in the combustion byproducts is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an exhaust system for use with a spark-ignited gaseous fuel internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the internal combustion engine system having exhaust system.    Internal combustion engine system (100)    Spark-ignited internal combustion engine (110)    Exhaust system (120)    Compressor (140)    Turbine (160)
NOVELTY - The method involves cooling first overhead stream (30) to entering into second fractionating column (15) through heat exchange with second overhead stream (40), low pressure stream (84), and intermediate pressure stream. The low pressure stream is compressed to pressure equal to that of intermediate pressure stream. The first compressed stream is compressed to pressure equal to that of high pressure stream (130), for combining two streams to form second compressed stream. The second compressed stream is compressed to produce high pressure methane product stream.    USE - Method for removing nitrogen and for producing high pressure methane product stream and natural gas liquid stream.    ADVANTAGE - The economical efficient removal of nitrogen from methane can be facilitated effectively. The generation of defects caused due to freeze-out problems can be eliminated effectively. The dramatic reduction in the overall compression requirements can be ensured. The power requirements for compressing methane product stream to produce suitably high pressure stream for sale can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the separation of nitrogen-methane portion.    Second fractionating column (15)    First overhead stream (30)    Second overhead stream (40)    Low pressure stream (84)    High pressure stream (130)
NOVELTY - Preparing an aryloxyalkylene amine compound via an aminoethylation reaction, comprises (a) reacting an aromatic hydroxyl compound in the presence of a basic catalyst with a 2-oxazolidinone compound (II) to form an intermediate reaction product, and (b) reacting the intermediate product with a polyalkylene polyamine.    USE - The process is useful for preparing aryloxyalkylene amine compound via aminoethylation reaction (claimed), where the aryloxyalkylene amine compound: is useful as raw materials for preparing pharmaceuticals and pesticides; and has antiinflammatory activity and analgesic activity. No biological data given.    ADVANTAGE - The process ensures economical production of the aryloxyalkylene amine compound with improved yield and without using large quantities of unwanted by-products.    DETAILED DESCRIPTION - Preparing an aryloxyalkylene amine compound via an aminoethylation reaction, comprises (a) reacting an aromatic hydroxyl compound in the presence of a basic catalyst with a 2-oxazolidinone compound of formula (II) to form an intermediate reaction product, and (b) reacting the intermediate product with a polyalkylene polyamine.    R3 = H or lower 1-6C-alkyl; and    R4 = H, straight or branched chain 1-6C-alkyl, phenyl, alkaryl, or arylalkyl.
NOVELTY - Method for preparing special fertilizer for corn, involves mixing human and animal excrement with 20-22% straw, 20-225 rape seeds, 8% lees, 1% organic fertilizer, 6% diammonium phosphate, 8% potassium sulfate, 10% bentonite, 0.4% magnesium, 0.1% zinc and 0.1% iron, crushing the mixture, adding water (suitable amount) to the crushed material, and composing the product in summer for 32-36 days, and in winter for 62-66 days, where the above-mentioned components except human and animal excrement are crushed in a crusher.    USE - The method is useful for preparing special fertilizer which is useful for corn (claimed).    ADVANTAGE - The method is simple. The fertilizer prepared by the method is rich in nutrition (trace elements).
NOVELTY - Producing base fertilizer for chestnut trees, involves (a) mixing human and animal excreta, hay and chestnut leaves, castor seed cake, sauce residue and river mud, and crushing and mixing with organic fertilizer leaven, and adding water and stirring uniformly, stacking and fermenting, and (b) mixing ammoniumnitrate, monoammonium phosphate, potassium chloride, magnesium sulfate, humic acid manganese chelate and borax, and crushing and mixing uniformly with fermented product to obtain the product.    USE - The method is useful for producing base fertilizer for chestnut trees (claimed), which is useful for promoting growth, improving drought resistance, quality of fruit, and anti-water logging, protecting flowers and fruits.    ADVANTAGE - The fertilizer is rich in organic matter, nitrogen, phosphorus, potassium and trace element, improves soil fertility, and slowly release nutrient element to Chinese chestnut tree.    DETAILED DESCRIPTION - Producing base fertilizer for chestnut trees, involves (a) mixing 25-27 wt.% human and animal excreta, 24-26 wt.% hay and chestnut leaves, 6 wt.% castor seed cake, 5 wt.% sauce residue and 15 wt.% river mud, and adding into crusher and crushing and mixing with 1 wt.% organic fertilizer leaven, and adding water and stirring uniformly, stacking and sealing the stack using thin plastic film and fermenting for 28-30 days in summer and 58-60 days in winter, and (b) mixing 6 wt.% ammoniumnitrate, 5 wt.% monoammonium phosphate, 6 wt.% potassium chloride, 3 wt.% magnesium sulfate, 0.5 wt.% humic acid manganese chelate and 2.5 wt.% borax, and adding into crusher and crushing and mixing uniformly with fermented product obtained in step (a) to obtain the product.
NOVELTY - Dome-shaped inflatable roof (2) comprises: a gas-tight and optionally liquid-tight backing sheet, which can be applied to the open top of a container shell having a circular basic shape; and a number of stabilizing elements (5), which interact load transmitting arrangement with a base film (4) and are used as derivation of tensile forces.    USE - The dome-shaped inflatable roof is useful for a biogas tank (1) (claimed).    ADVANTAGE - The dome-shaped inflatable roof: has simple construction; and exhibits high strength.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic top view of the biogas tank with dome-shaped inflatable roof.    Biogas tank (1)    Inflatable roof (2)    Base film (4)    Stabilizing elements (5)    Pole (7)
NOVELTY - Method for performing quantitative fermentation of Ganoderma notoginseng mycoplasma, involves using pseudoginseng residue as raw material, preprocessing by drying pseudoginseng residue after sieving, preparing and mixing the preprocessed pseudoginseng residue, nitrogen source, phosphorus source, bran and water, uniformly mixing, sterilizing the mixed material, fermenting by inoculating 10-20% mixed fermenting strain, preferably Ganoderma lucidum, and culturing to obtain product.    USE - The method is useful for performing quantitative fermentation of Ganoderma notoginseng mycoplasma which is used for adjusting and strengthening immunity of human body, delaying aging, relieving cough and asthma, resisting fatigue, resisting tumor, resisting liver damage, treating cardiovascular disease, rheumatic disease, rheumatoid disease, and neurasthenia (all claimed).    ADVANTAGE - The method prepares product which exhibits odor removal function, and reduces the environment pollution.    DETAILED DESCRIPTION - Method for performing quantitative fermentation of Ganoderma notoginseng mycoplasma, involves using pseudoginseng residue as raw material, preprocessing by drying pseudoginseng residue after sieving, preparing and mixing the 100 pts. wt. preprocessed pseudoginseng residue, 0-6 pts. wt. nitrogen source, 0-0.6 pts. wt. phosphorus source, 0-20 pts. wt. bran and water, uniformly mixing, where the mass ratio of solid material and water is 1:1.5-1:2, mixing uniformly, sterilizing the mixed material by performing high pressure steam sterilization with the steam pressure of 1 atm at 121 degrees C for 30 minutes, fermenting by inoculating 10-20% mixed fermenting strain, preferably Ganoderma lucidum under normal pressure at 24-28 degrees C for 10-16 days, and culturing to obtain product.
NOVELTY - Treatment of acidic methyl cellulose condensate comprises transferring condensate into sedimentation tank, neutralizing at pH 6.5-7.5 using 15% sodium carbonate solution, adding 10% fertilizer solution, reacting in biological membrane anaerobic reactor, collecting methane, discharging sludge to sludge thickening tank and dewatering sludge using frame filter press.    USE - Method for treating acidic methyl cellulose condensate (claimed).    ADVANTAGE - The method is inexpensive, efficient and energy-saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of acidic methyl cellulose condensate treatment (Drawing includes non-English language-text).
NOVELTY - Preparing rosuvastatin calcium intermediate comprises adding 4-(4-fluorophenyl)-6-isopropyl-2-(N-methyl-n-methylsulfonyl)amino)pyrimidine-5-yl-methanol into a solvent, cooling to -5 to 10 degrees C, and adding R-3-(tert-butyldimethylsilyloxy)-5-oxo-6-triphenylphosphoranylidenehexanoate, then adding nano-nickel powder, reacting at 50-80 degrees C for 15-24 hours, filtering, vacuum concentrating the filtrate, and then placing the residue on a silica gel column, eluting with chloroform, and vacuum concentrating.    USE - The method is useful for preparing rosuvastatin calcium intermediate (claimed).    ADVANTAGE - The method uses simple raw materials, has mild reaction conditions, is environmentally friendly, and suitable for large-scale industrial production.    DETAILED DESCRIPTION - Preparing rosuvastatin calcium intermediate comprises adding 4-(4-fluorophenyl)-6-isopropyl-2-((N-methyl-n-methylsulfonyl)amino)pyrimidine-5-yl-methanol into a solvent, cooling to -5 to 10 degrees C, and adding R-3-(tert-butyldimethylsilyloxy)-5-oxo-6-triphenylphosphoranylidenehexanoate, where the molar ratio of 4-(4-fluorophenyl)-6-isopropyl-2-((N-methyl-n-methylsulfonyl)amino)pyrimidine-5-yl-methanol and R-3-(tert-butyldimethylsilyloxy)-5-oxo-6-triphenylphosphoranylidenehexanoate is 1:1-1.05, then adding nano-nickel powder (NiNP), where the mass ratio of 4-(4-fluorophenyl)-6-isopropyl-2-((N-methyl-n-methylsulfonyl)amino)pyrimidine-5-yl-methanol with NiNPs is 1:0.1-0.2, reacting at 50-80 degrees C for 15-24 hours, filtering, vacuum concentrating the filtrate, and then placing the residue on a silica gel column, eluting with chloroform, and vacuum concentrating to obtain 7-(4-(4-fluorophenyl)-6-isopropyl-2-(N-methyl-N-methylsulfonylamino)pyrimidin-5-yl)-(3R)-3-(tert-butyldimethylsilyloxy)-5-oxo-6-heptanoate.
NOVELTY - Bio-organic fertilizer fermenting microbial inoculum comprises Amylomyces rouxii, Penicillium cordubense and Bacillus phychrophilus.    USE - As bio-organic fertilizer fermenting microbial inoculum.    ADVANTAGE - The microbial inoculum rapidly improves pile temperature, shortes fermentation period, and can effectively kill pathogens in animal feces and parasites. The fertilizer is rich in nutrient content.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing biological fermentation organic fertilizer, which involves crushing crop straw and livestock and poultry excrement, adjusting carbon/nitrogen ratio to 28-32 and water content to 60-65%, adding the microbial inoculum, stacking the mixture at 55 degrees C, turning, and performing aerobic high temperature fermentation after 20-30 days; and    (2) fertilizer prepared by the method.
NOVELTY - Straw microbial degradation agent comprises 1x 103-5x 104 colony-forming unit (cfu)/ml Trichoderma and 5x 108-1x 1010 cfu/ml Pseudomonas strains B6-15.    USE - The microbial degradation agent is useful for promoting growth of crop straw, and improving crop soil characteristics (all claimed).    ADVANTAGE - The agent can substantially decay straw at 20-25 degrees C for 15 days, and provides degradation rate of more than 58%. The agent is suitable for northern area under low temperature environment, and provides high thallus growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent, which involves (a) inoculating Trichoderma and Pseudomonas strain B6-15 into solid culture medium under aseptic condition and activating strain, (b) inoculating activated strain into liquid culture medium under aseptic condition at 150-180 revolutions per minute (rpm), and (c) inoculating obtained strain into liquid culture medium, and culturing medium.
NOVELTY - The utility model claims fermentation for producing biological fertilizer by waste's device, composed of a frame, a water storage tank, a water injection port, a movable bottom plate, a crushing box, tank feeding port, crushing box, a spray head, a bent head, a crushing box discharge hole, constant temperature drying box, a fan, a, constant temperature pipe, a water outlet, a discharge outlet, a transmission gear, a motor, a universal wheel. Said device is upper, middle and lower layer structure, the upper part is a water storage tank, the bottom's in the water storage tank is provided with a water box movable plate, middle part is a crushing box, crushing main shaft is provided with a plurality of upper blade, discharge hole is connected with the constant-temperature tank with the air feeding port corresponding to the constant-temperature drying box the device's lower part, the bottom is provided with a constant temperature pipe, the water outlet is provided with a water outlet on the left side of the upper part is provided with, the top is provided with a fan, the four corners of the bottom of the frame is provided with a universal wheel, the device is featured with simple structure and convenient use and so on, it's good popularization and use value.
NOVELTY - Preparing N-H or N-alkyl 2-propynamides (I), involves reacting a propiolic acid ester with an amine, in water, and at a reaction temperature of -10 degrees C to 10 degrees C to form the compound (I).    USE - For preparing N-H or N-alkyl 2-propynamides (claimed) which are useful as intermediate in the manufacture of pharmaceutical ingredients.    ADVANTAGE - The method provides desired product in high quality, high purity and good chemical yield, and in an efficient and environmentally friendly manner; does not require the use of low temperatures or organic solvents; and allows to produce the desired product efficiently with good control of the quality.    DETAILED DESCRIPTION - Preparing N-H or N-alkyl 2-propynamides of formula (I), involves reacting a propiolic acid ester of formula (II) with an amine of formula (III), in water, and at a reaction temperature of -10 degrees C to 10 degrees C to form the compound (I).    R1=H or 1-4C alkyl;    R2=1-2C alkyl.
NOVELTY - A methanation catalyst contains 65-88 mass% aluminum oxide as catalyst carrier, 12-18 mass% nickel as active ingredient, 0-20 mass% zirconium component, and 0-5 mass% transition metal.    USE - A methanation catalyst for carbon monoxide (claimed).    ADVANTAGE - Catalyst is low-cost, has excellent carbon monoxide methanation catalytic activity and hydrothermal stability, high specific surface area, pore volume, pore size distribution, and conversion rate, and suitable for high-speed operation and preparation process is easy, simple, and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanation catalyst which involves mixing nickel, aluminum oxide, zirconium component, and transition metal soluble salt into dispersant to obtain solution, precipitating at 40-80 degrees C through lye as precipitating agent and adjusting pH value to 8-10, aging for 6-24 hours, performing suction filtration, washing with water, adjusting pH of component to less than or equal to 7, drying to 80-110 degrees C for 6-12 hours, and calcining at 350-950 degrees C for 1-6 hours.
NOVELTY - A 1-(chloroacetyl)-2-(trifluoroacetyl)hydrazine is prepared by mixing ethyl trifluoroacetate and hydrazine hydrate, adding solvent, reacting, adding acid-binding agent and chloroacetyl chloride, and concentrating.    USE - Method for preparing 1-(chloroacetyl)-2-(trifluoroacetyl)hydrazine used for pharmaceutical intermediate (claimed).    ADVANTAGE - The raw materials are easy to obtain. The product is low-cost and environment-friendly. The method is simple, energy efficient and suitable for industrialization. It has high product yield, good purity and stable quality.
NOVELTY - This utility model claims one kind of forest green garbage processing system, comprising a fermenting tank and green by system, said green using system comprises a land system, water supply system and cultivation system, said land system, water supply system and upper system for stable covering layer. The utility model can effectively processing organic waste and producing fertilizer, earthworm and so on. Reduces the land maintenance cost, small floor space, underground water pollution, harmless and resource, reduction and the dry branches and fallen leaves in autumn is no longer the environment, domestic garbage is not filled, has good economic benefit and social benefit's, which is good for popularization and application.
NOVELTY - Preparing synthesis gas involves double-mode biomass gasification/reforming process. Solid material is filled into biomass gasifier. Partial oxidation gasification of the solid material is carried out in gasifier in presence of oxygen to obtain a product. Biomass pyrolysis of the obtained product is carried out to generate pyrolysis product. Partial oxidation gasification and pyrolysis product is heated at 600-800 degrees C in presence of nickel-based catalyst into a steam reforming to generate pure synthesis gas, which comprises hydrogen, carbon monoxide, methane and carbon dioxide gas.    USE - Method for preparing synthesis gas (claimed).    ADVANTAGE - The method enables to prepare pure synthesis gas is easy to control and applied to obtain high added value products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nickel-base catalyst which involves:    (A) mixing a precursor solution of the precursor and co-catalyst metal of the main catalyst into de-ionized water to obtain a mixture;    (B) heating and stirring the mixed product, then drying to obtain a catalyst precursor;    (C) heating the catalyst precursor at 300 degrees C for 2 hours in presence of oxygen, then heating the catalyst precursor at 600 degrees C for 3 hours to obtain a primary catalyst; and    (D) treating the primary catalyst with hydrogen before use.
NOVELTY - The composite hollow fiber membrane comprises an ultrafiltration membrane surface made of glassy polymer material or polyethylene propylene glycol, where the film is coated with organopolysiloxane copolymer in which a recurring unit is grafted.    USE - The composite hollow fiber membrane is useful for separating carbon dioxide and methane in a purification process of a biogas (claimed) such as bio methane.    ADVANTAGE - The hollow fiber composite membrane has improved permeability of the carbon dioxide, selectively removes the carbon dioxide of the biogas purification process from the mixed gas of the carbon dioxide/methane, and improves the separation efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a membrane module including a hollow fiber composite membrane; and    (2) manufacturing a hollow fiber composite membrane comprising providing a spinning solution to a the hollow fiber membrane, radiating through a spinneret, adding an additive with the spinning solution, stirring uniformly, dissolving the glassy polymer in the solution to obtain an organic solvent, and coating a recurring unit with the grafted organopolysiloxane copolymer solution including polyethylene glycol.
NOVELTY - The tool has an actuating mechanism that is connected with measuring equipment and provided to control mode of operation of a gas piston power unit and a gasifier. An air supply regulator is provided to regulate the air supplied into the gas piston power unit. A mixer is provided to mix the exhaust gases obtained from the gas piston power unit and the gases obtained from the gasifier, and connected with an ignition device.    USE - Power-engineering tool for processing of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the power-engineering for processing of biomass.
NOVELTY - Synthesis of 17- alpha -hydroxyprogesterone (V) comprises performing acetone cyanohydrin addition of androstenedione (I) with 17 carbonyl group, constructing 17-hydroxy-17-cyano-chiral carbon atom compound to obtain 17- alpha -hydroxy-17- beta -cyano-androst-4-ene-3-one (II), protecting to obtain 3-carbonyl protected compound (III), taking protection to obtain 17- alpha -hydroxyl protected compound (IV), performing methylation and hydrolyzing.    USE - Method for synthesizing 17- alpha -hydroxyprogesterone (V) (claimed).    ADVANTAGE - The method has high yield, good selectivity, low cost, moderate reaction conditions and no pollution. It is stable and suitable for industrial production.    DETAILED DESCRIPTION - Synthesis of 17- alpha -hydroxyprogesterone of formula (V) comprises performing acetone cyanohydrin addition of androstenedione of formula (I) with 17 carbonyl group, constructing 17-hydroxy-17-cyano-chiral carbon atom compound to obtain 17- alpha -hydroxy-17- beta -cyano-androst-4-ene-3-one of formula (II), protecting to obtain 3-carbonyl protected compound of formula (III), taking protection to obtain 17- alpha -hydroxyl protected compound of formula (IV), performing methylation and hydrolyzing.
NOVELTY - An algal biomass pyrolysis device comprises fast pyrolysis bed (1), circulating fluidized bed (2), pyrolysis bed material returning valve (3), fluidized bed material returning valve (4), pyrolysis bed gas-solid separator (5), fluidized bed gas-solid separator (6), gas-liquid separator (7), oil-water separator (8), bio-oil storage tank (9), non-condensable gas storage tank (10) and tail part heating surface (11).    USE - Algal biomass pyrolysis device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of algal biomass pyrolysis device.    Fast pyrolysis bed (1)    Circulating fluidized bed (2)    Pyrolysis bed material returning valve (3)    Fluidized bed material returning valve (4)    Pyrolysis bed gas-solid separator (5)    Fluidized bed gas-solid separator (6)    Gas-liquid separator (7)    Oil-water separator (8)    Bio-oil storage tank (9)    Noncondensable gas storage tank (10)    Tail part heating surface (11)
NOVELTY - Environment-friendly odorless toilet excrement fermentation comprises mixing sawdust, rice husk, rice powder, wheat powder, broomcorn powder and/or mulberry powder with solution of fermentation agent or fermentation initiator and water, adding corn powder and bran, introducing into fermentation barrel, covering with film, fermenting for 3-7 days, and arranging in sanitary toilet or stool barrel. A pad is arranged on bottom of stool barrel, stool is covered with fermented material after defecation, and stool barrel is continuously used until full, replacing new material pad bottom.    USE - Method for toilet excrement fermentation used for producing organic fertilizer for vegetables, fruit trees, grass and edible mushroom (claimed).    ADVANTAGE - The method is environment-friendly and solves water pollution problem.    DETAILED DESCRIPTION - Environment-friendly odorless toilet excrement fermentation comprises mixing sawdust, rice husk, rice powder, wheat powder, broomcorn powder and/or mulberry powder; mixing 100 kg sawdust mixture with 20 kg 1% solution of fermentation agent having activity of 99% or 20 g fermentation initiator and 20 kg water; adding 1 kg corn powder and bran in summer or 2 kg corn powder and bran in winter; introducing into fermentation barrel; covering with film; fermenting for 3-7 days; and arranging in sanitary toilet or stool barrel. A pad is arranged on bottom of stool barrel, stool is covered with fermented material after defecation, and stool barrel is continuously used until full, replacing new material pad bottom. An INDEPENDENT CLAIM is included for a toilet excrement fermentation barrel comprising stainless steel barrel, pedestal pan, material barrel, pedal switch, and quantitative spraying device.
NOVELTY - A rice composite microorganism fertilizer comprises 0.1-20 pts. wt. humic acid rare earth mixture, 0.01-1 pt. wt. polyaspartic acid, 0.1-10 pts. wt. silicon-calcium-magnesium fertilizer, 0.1-10 pts. wt. amino acid fertilizer, 0-40 pts. wt. nitrogen-phosphorus-potassium fertilizer and 14-97 pts. wt. fermented organic matter.    USE - Rice composite microorganism fertilizer.    ADVANTAGE - The fertilizer having high biological activity improves resistance and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fermented organic matter comprising fermenting culture material comprising Bacillus subtilis, hull powder or peanut shell, wheat bran, soybean cake powder, corn powder, magnesium sulfate, manganese sulfate, and fermentation material comprising water, grass or straw, and livestock excrement.
NOVELTY - Preparation of dendrobe substrate comprises spreading straw layer, buffer layer and substrate layer, adding water, inoculating with effective microorganism bacteria, piling, fermenting for 20-25 days and sterilizing. The buffer layer comprises excrementum bombycis, edible fungi culture material, river sand, brown sugar, weathered coal, wintergreen oil and rice bran. The substrate layer includes dry animal feces, bark powder, peanut shell, bran, fruit slag, iron ore slag, quicklime, nanocarbon, wintergreen oil, attapulgite, brick dregs, borax and sodium selenite.    USE - Method for preparing dendrobe substrate (claimed).    DETAILED DESCRIPTION - Preparation of dendrobe substrate comprises spreading straw layer, buffer layer and substrate layer, adding water, inoculating with effective microorganism bacteria, piling, fermenting for 20-25 days and sterilizing. The buffer layer comprises 12-15 pts. wt. excrementum bombycis, 100-120 pts. wt. edible fungi culture material, 50-60 pts. wt. river sand, 1-2 pts. wt. brown sugar, 12-15 pts. wt. weathered coal, 1-2 pts. wt. wintergreen oil and 20-25 pts. wt. rice bran. The substrate layer comprises 200-300 pts. wt. dry animal feces, 140-180 pts. wt. bark powder, 40-50 pts. wt. peanut shell, 20-30 pts. wt. bran, 60-70 pts. wt. fruit slag, 15-20 pts. wt. iron ore slag, 1-2 pts. wt. quicklime, 1-2 pts. wt. nanocarbon, 1-2 pts. wt. wintergreen oil, 30-40 pts. wt. attapulgite, 80-90 pts. wt. brick dregs, 0.1-0.2 pt. wt. borax, 0.2-0.3 pt. wt. sodium selenite, 0.02-0.03 pt. wt. acid, 0.02-0.03 pt. wt. manganese acetate, 0.2-0.3 pt. wt. ferrous sulfate and 0.1-0.2 pt. wt. zinc sulfate.
NOVELTY - Capturing biogas from nejayote involves utilizing anaerobic digester containing mesophilic and thermophilic microorganisms. Methane content of the biogas produced from multiple organic materials is subjected to anaerobic digestion in anaerobic digester. Carbon dioxide is provided as a carbon source.    USE - Method for capturing biogas from nejayote.
NOVELTY - An organic acid extract or liquor is produced by leaching decomposed or decomposable naturally occurring organic material, such as compost, with a biological liquid under controlled pH and temperature conditions for a predetermined period, and separating the liquid from the organic material. The resulting extract or liquor contains soluble humate.    USE - Method of producing organic acid extract or liquor used as biological fertilizer (claimed).    ADVANTAGE - The method can produce an organic acid extract or composition without use of chemicals such as potassium hydroxide in production. It involves use of an acid extraction environment to yield proportionally more fulvic acid or fulvates when compared to an alkaline extraction technique. The resulting liquor has humate concentration of 3-18%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic acid extract or liquor.
NOVELTY - The earthworm flowerpot support comprises a main body in which an upper side is opened, an earthworm chamber, an earthworm cast in which an inner portion absorbs resides of food waste, a moving hole, a garbage chamber having the food waste, multiple seed balls, a water ball, and a member configured for opening and closing the earthworm chamber. An inner portion of the main body is inserted into the chamber. The multiple seed balls are placed in a side of the main body. The water ball is placed in a lower side of the support. The main body has a drain-pan.    USE - The earthworm flowerpot support is useful for processing food waste (claimed) of home or office.    ADVANTAGE - The support effectively processes the food waste without undesirable odor.    DETAILED DESCRIPTION - The earthworm flowerpot support comprises a main body in which an upper side is opened, an earthworm chamber, an earthworm cast in which an inner portion absorbs resides of food waste, a moving hole, a garbage chamber having the food waste, multiple seed balls, a water ball, and a member configured for opening and closing the earthworm chamber. An inner portion of the main body is inserted into the chamber. The multiple seed balls are placed in a side of the main body. The water ball is placed in a lower side of the support. The main body has a drain-pan equipped at a lower side of the support. The opening and closing member includes a door, and an insertion hole. The insertion hole is connected with the garbage chamber. The opening and closing member and the earthworm chamber are attached and detached in a velcro.
NOVELTY - This utility model claims a kind of organic material fermentation for conveying belt, comprising a conveying belt, a flange of the conveyer belt with wavy retaining edge is set with two sides of the base band, the upper and base band are provided with air holes. The width of the band conveyor belt is 500 to 3000, the flange is 20 to 800 , the width of the distance base band outer side is less than 200. At the same time in order to prevent the flange overturning side of the two conveying belt between the flanges is provided with reinforcing rib. And the utility model is air hole set on base and , which effectively improves organic material in the air condition is fermentation organic material is a dynamic aerobic fermentation, accelerating fermentation material water evaporation, which obviously improves the fermentation efficiency of the organic material and shortens fermentation period.
NOVELTY - A kind of UASB reactor, comprising a reactor tank body, a water inlet, the bottom of the reactor, the reactor is provided with the tank body from bottom to top is in turn connected with a sludge bed, suspension cell, and precipitation reaction region, the deposition on the reaction area is provided with a connected with the marsh gas collecting area, a marsh gas collecting area is provided with an exhaust port, the water inlet is connected with the sludge bed, the deposition in the reaction zone is provided with a three-phase separator, the upper end of the three-phase separator is provided with inclined to form a inclined settling zone. This utility model by adding biological filler in suspending area to make the microorganism in the sewage with the carrier, it will not loss the water, which can effectively improve the MLSS, the residence time is prolonged, so a higher pollutant processing efficiency, at the same time through the inclined pipe in the sedimentation reaction area, which effectively improves the precipitation effect of the suspended solid is greatly reduced, the subsequent sewage treatment load to achieve more ideal treatment effect.
NOVELTY - A Corynebacterium lubricantis strain Phe-05 deposited as CCTCC NO: M2012031, is new.    USE - The strain is useful in microbial inoculum for biological treatment of phenol containing industrial wastewater (claimed).    ADVANTAGE - The strain degrades phenol in wastewater by simple and highly efficient process at low cost, and causes no secondary pollution.
NOVELTY - This utility model claims a kind of automatic environmental friendly organic material fermentation system, comprising a fermentation conveyor unit, fermenting conveyor unit is provided with multiple groups of, each group is composed of a plurality of fermentation conveyor layering according to the order from low to high is set with solid form, is equipped with several straight line connected with the fermentation material conveyor, the material from the input end of fermentation conveyor unit is high and the fermentation, wherein the fermentation from high to low layer conveying is reduced during the process, the output by the output end of the conveyor for the low layer. This utility model uses a three-dimensional layered design, to make the material ferment workshop use rate, the fermentation efficiency is greatly improved, at the same time, carrying out a process of odour to realize clean and environment-friendly production, solves the problem that the traditional technology in the prior art.
NOVELTY - A kind of new-style hole plate type dividing device for marsh gas treatment system for food waste treatment, comprising a marsh gas voltage regulation cabinet, a biogas pressure stabilizing cabinet is provided with a first air outlet and a second air outlet pipe, the first air pipe and the second air outlet pipe are provided with a valve and a gas flow meter, a gas outlet pipe and a methane burner is connected with a gas outlet pipe and a marsh gas biological desulphurization system. This utility model solves the problem that the existing technology is difficult to kitchen garbage generated for process and effective use by carrying out a series of processing to marsh gas and achieve good treatment and effective utilization of the marsh gas.
NOVELTY - This utility model claims a kind of marsh gas pool auxiliary-increasing device, the wind power above the ground blows wind power generator blade of the wind driven generator rotating shaft to rotate to drive the wind power generator by a direct current motor, the direct current wire is adjusted by a controller, then the input inverter into alternating current power, alternating current drive motor drives the stirrer in the fermentation liquor in the fermentation of the marsh gas tank, continuously stirring in the fermentation in the marsh gas pool of ferment liquid to make the fermentation liquid and the methane bacteria in the fermentation of fully stirring, promote the growth and propagation of methane bacteria, obviously improves the production efficiency of the fermentation liquor, and the other part of the first alternating current power input is provided with the heating device in the fermentation liquor in the fermentation, the electric energy is converted into heat energy, the methane bacteria in proper temperature environment produce more marsh gas.
NOVELTY - This utility model belongs to marsh gas equipment fittings technology field, especially relates to a kind of improved structure of marsh gas tank. It solves the technical problem that the design of the present technology is not reasonable enough and easy to block and so on; The improved structure of biogas tank comprises a fermentation chamber of the box body is provided with a connected with the fermentation chamber of the feeding pipe and the discharging pipe on the side part of the box body, one end of the feeding pipe of the feeding end, and the other end is a discharging end, wherein the box body or a tube in the feeding pipe is provided with a discharging end of the drawing mechanism. Compared with the existing technology, the utility model is novel in the design is more reasonable, the structure is simple, the practicability is strong, besides, a continuity is good, it is not easy to be blocked and long service life, and meets the social skill development;
NOVELTY - This utility model claims a refuse landfill. pumping well, comprising a suction pipe, a flow control valve, a connecting pipe and the through hole pipe, and from top to bottom in turn is provided with a clay, bentonite layer, a sealing ring, a soil engineering cloth and gravel layer, the through hole is placed in the gravel layer, the two sides of the air pipe is provided with a monitoring port and a temperature sensor. This utility model is capable of effectively extracting the landfill garbage landfill, comprising pumping well sealing structure, convenient operation and maintenance, and it can control the gas flow rate.
NOVELTY - Method for degrading cellulose under anaerobic condition for producing methane, involves obtaining straw, industrial wastewater, domestic sewage and poultry and livestock excrement as fermentation substrate, dissolving calcium pantothenate and tetrahydrofolic acid in water or biogas slurry to obtain mixed solution, introducing the marsh gas into fermentation raw material, adding livestock manure as inoculum, mixing uniformly and then carrying out anaerobic fermentation.    USE - The method is useful for degrading cellulose under anaerobic condition for producing methane (claimed).    ADVANTAGE - The method is simple and cost-effective, and improves degradation efficiency and output of cellulose.
NOVELTY - Processing corn straw using malic acid methyl morpholine oxide (NMMO), involves carrying malic acid-NMMO-water pretreatment system by mixing ???0, malic acid, and deionized water, treating mixture, regenerating cellulosic material, washing regenerated cellulosic material three times with deionized water, adjusting pH of the mixture to 4.8 by adding citrate-sodium buffer to obtain mixture, where final concentration of corn straw and cellulase enzyme are 2% and 0.2% respectively, oscillating the mixture, and obtaining product.    USE - The method is useful for processing corn straw (claimed).    ADVANTAGE - The method is simple, and high in efficiency, and reduces sugar yield to not less than 62% due to usage of NMMO and corn straw.    DETAILED DESCRIPTION - Processing corn straw using malic acid methyl morpholine oxide (NMMO), involves carrying malic acid-NMMO-water pretreatment system by mixing 85 %mass ???0, 0.3-10 %mass malic acid, and 5-14.7 %mass deionized water, treating mixture at 95-130 degrees C for 0.5-2 hours, regenerating cellulosic material, washing regenerated cellulosic material three times with deionized water, adjusting pH of the mixture to 4.8 by adding 50 mM citrate-sodium buffer to obtain mixture, where final concentration of corn straw and cellulase enzyme are 2% and 0.2% respectively, oscillating the mixture at 50 degrees C and 150 rotations per minute (rpm) using shaker, and obtaining product.
NOVELTY - Processing corn straw, involves mixing N-Methylmorpholine N-oxide (???0), sodium dodecyl sulfate (SDS), citric acid and deionized water, dissolving corn straw in mixture, washing the corn straw with deionized water, regenerating cellulose material, washing regenerated cellulosic material three times with deionized water, adding 50 mM citric acid-sodium citrate buffer (pH 4.8) to the corn straw, adding 0.2% cellulase enzyme to mixture, hydrolyzing the mixture at 50 degrees C under stirring at 160 rotations per minute (rpm), and obtaining processed corn straw.    USE - The method is useful for processing corn straw (claimed).    ADVANTAGE - The processed corn straw has high voltage value, and reduces sugar yield to not less than 63%. The method is simple, and highly efficiency, and produces low waste.    DETAILED DESCRIPTION - Processing corn straw, involves mixing 85 %mass N-Methylmorpholine N-oxide (???0), 0.3-5 %mass sodium dodecyl sulfate (SDS), 0.3-5 %mass citric acid and 5-14.4 %mass deionized water, dissolving corn straw in mixture at 95-130 degrees C for 0.5-2 hours, washing the corn straw with deionized water, regenerating cellulose material, washing regenerated cellulosic material three times with deionized water, adding 50 mM citric acid-sodium citrate buffer (pH 4.8) to the corn straw, adding 0.2% cellulase enzyme to mixture, hydrolyzing the mixture at 50 degrees C under stirring at 160 rotations per minute (rpm), and obtaining processed corn straw.
NOVELTY - Recovery of sulfur comprises (A) roasting gold concentrate to obtain flue gas, adding sodium hydroxide solution; (B) diluting with water to obtain sulfite ion; (C) adding to anaerobic fermentation reactor with sulfate-reducing bacteria, and reverting sulfite ion to hydrogen sulfide; (D) mixing with roasting gold concentrate flue gas to obtain elemental sulfur; and (E) subjecting fermentation broth to solid-liquid separation, returning active microorganisms-containing sludge to anaerobic reactor to carrying out increase anaerobic fermentation; and separating wastewater and water.    USE - Method for recovery of sulfur (claimed).    DETAILED DESCRIPTION - Recovery of sulfur comprises (A) roasting gold concentrate to obtain flue gas, adding sodium hydroxide solution to obtain sodium sulfite solution; (B) diluting with water to obtain less than 1% sulfite ion; (C) adding to anaerobic fermentation reactor with sulfate-reducing bacteria, and reverting sulfite ion to hydrogen sulfide; (D) mixing with roasting gold concentrate flue gas to obtain elemental sulfur; and (E) subjecting fermentation broth to solid-liquid separation, returning active microorganisms-containing sludge to anaerobic reactor to carrying out increase anaerobic fermentation; and separating wastewater and water.
NOVELTY - Efficient hydrolysis reactor, comprising a base on the bottom of the reactor of the activated sludge bed and a bio-membrane bed of the upper part of the reactor, further comprising a sewage and a water inlet pipe of the waste water, a water inlet pipe connected with the water distributing pipe, the water outlet of the water distribution pipe is located at the bottom of the active sludge bed, further comprising an air inlet pipe, an air inlet pipe is connected with the back-washing air pipe is connected, a reverse washing air pipe is an air outlet located on the active sludge and bio-membrane bed biological film bed is set above the water outlet weir plate. According to the high-efficient hydrolysis reactor also comprises a ventilating element for exhausting pipe of the bio-membrane is adhered to the suspension of bio-membrane bed of gas and death from falling off, discharging pipe connected with the lower part of the air inlet pipe. By a large resistance water distribution system with multi-flow water weir system, a water distribution uniformity without dead zone so as to improve the mass transfer efficiency of the system and improve the biochemical reaction speed to realize the high efficiency of the organic matter.
NOVELTY - Extracting 11a-hydroxy-16,17a-epoxyprogesterone comprises mixing methoxydienone and mycelium mixture with toluene and chloroform mixed solution, raising the temperature to completely dissolve, carrying out solid-liquid separation, concentrating the filtrate, refining, carrying out secondary solid-liquid separation, adding toluene-chloroform mixed solution, separating the solid, raising the temperature to completely dissolve, carrying out solid-liquid separation, concentrating and refining the filter cake after the secondary solid-liquid separation, and separating.    USE - The method is useful for extracting 11a-hydroxy-16,17a-epoxyprogesterone (claimed).    ADVANTAGE - The method has simple extraction process, requires less equipment, and reduces the production cost and environmental pollution.
NOVELTY - Phenolic pollutants are metabolically decomposed by dosing phenolic-pollutant-containing water body with decreasing concentrations of substrate solution with ratio initial substrate solution dose:phenolic pollutants of 10-500:1 and dosing interval of 1-7 days in which amount of subsequently added substrate solution is 1/10-1/90 of the amount of previously added substrate solution.    USE - Metabolic decomposition of phenolic pollutants (claimed).    ADVANTAGE - Metabolic decomposition of phenolic pollutants saves consumption of substrate and has flexible operation, low operating cost, and good treatment effect.
NOVELTY - The tank has a biogas collecting pipe (4) that is paved with a bottom on the inner wall of the concrete tank main portion (1) and the bottom film (2). The bottom film is fixed on the top edge of the concrete vat unit. The top portion of the concrete tank main portion is covered with a top film (3). The top film and the bottom film are fixed on the outer edge of the tank main portion. The biogas collecting pipeline is connected with the inner bottom of the inner wall of the concrete tank main portion. The bottom film and the top film are made of polyethylene.    USE - Anaerobic gas storage tank for processing poultry and livestock excrement sewage (claimed).    ADVANTAGE - The tank structure is simplified. The need to establish the other storage facility can be avoided. The investment can be saved. The processing of poultry and livestock in dung surface is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing poultry and livestock excrement sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic gas storage tank.    Concrete tank main portion (1)    Bottom film (2)    Top film (3)    Biogas collecting pipe (4)    Liquid dung surface (5)
NOVELTY - Ethyl 4-(acetyloxy)-2-ethoxybenzoate derivatives (I) as 2-ethoxy-4-amino-5-chloro-benzoic acid intermediates, are new.    USE - (I) are useful as intermediates for preparing 2-ethoxy-4-amino-5-chloro-benzoic acid (claimed).    ADVANTAGE - The method utilizes cheap and easily obtainable raw materials; has short synthetic route, mild reaction conditions, simple operation, less pollution and high yield; produces stable product with high purity; and is economical and suitable for industrial production.    DETAILED DESCRIPTION - Ethyl 4-(acetyloxy)-2-ethoxybenzoate derivatives of formula (I) as 2-ethoxy-4-amino-5-chloro-benzoic acid intermediates, are new.    R = H or Cl.    INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) preparing 2-ethoxy-4-amino-5-chloro-benzoic acid, comprising hydrolyzing (I).
NOVELTY - An additive composition comprises antioxidant and bio-enzyme, where weight ratio is 1:0.1-10. The antioxidant is hindered phenol, dual-hindered phenol, para-phenylene, single hindered phenol, and/or p-phenylenediamine. The biological enzyme comprises alcohol oxidase, aldehyde oxidase, amine oxidase, sulfhydryl oxidase, mercaptan, methyl naphthoquinone oxidase, peroxidase, demethylase, decarboxylase, aldolase, lyase, mercapto, desulfurization demethylase, ferrochelatase, cobalt chelatase, magnesium chelatase, and alcohol, acid and ester dehydratase.    USE - Additive composition used for improving biodiesel performance (claimed).    ADVANTAGE - The composition improves oxidation stability of biological diesel oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of additive composition comprising mixing raw materials at 60 degrees C.
NOVELTY - Diesel fuel additive composition comprises: lubricity improvers comprising fatty acid, fatty acid salts, fatty acid amides or fatty acid esters; biodiesel comprising fatty acid methyl ester of soybean oil, rapeseed oil or corn oil; and biological enzymes e.g. aldehyde oxidase, amine oxidase, sulfhydryl oxidase, methyl mercaptan oxidase, methyl naphthoquinone oxidase, peroxidase, demethylase, decarboxylase, aldolase, oxygen lyases, alcohols, acids, esters dehydratase, sulfo enzyme and sulfhydryl enzyme.    USE - Used as diesel fuel additive composition.    ADVANTAGE - The fuel additive composition has reduced sulfur content, and improved performance characteristics.    DETAILED DESCRIPTION - Diesel fuel additive composition comprises: lubricity improvers comprising fatty acid, fatty acid salts, fatty acid amides or fatty acid esters; biodiesel comprising fatty acid methyl ester of soybean oil, rapeseed oil or corn oil; and biological enzymes comprising aldehyde oxidase, amine oxidase, sulfhydryl oxidase, methyl mercaptan oxidase, methyl naphthoquinone oxidase, peroxidase, demethylase, decarboxylase, aldolase, oxygen lyases, alcohols, acids, esters dehydratase, sulfo enzyme, sulfhydryl enzyme, methyl desulfurization enzyme, ferrochelatase, and trace amount of chelated cobalt and magnesium chelatase. The weight ratio of the lubricity improver, the biodiesel and the enzyme is 1:0.1-10:0.1-10.
NOVELTY - Biogas slurry ecological purification based on microalgae cultivation, comprises: (1) biogas slurry pretreatment; (2) habituated culture of autotrophic microalgae, namely, obtaining algae strains capable of rapidly growing in 70-100% biogas slurry; (3) preparation of a seed solution; (4) a biogas slurry purification method during growing of microalgae; (5) biochemical breaking of microalgae cell walls; and (6) collection of the microalgae cells and recycling of the biogas slurry.    USE - The method is useful for biogas slurry ecological purification based on microalgae cultivation (claimed).    ADVANTAGE - According to the method, not only is a method provided for purifying the biogas slurry, but also the obtained algae cells and the biogas slurry can be recycled, so that ecologicalization treatment of the biogas slurry is realized, the environment is improved, and furthermore, the economic and social benefits are produced.    DETAILED DESCRIPTION - Biogas slurry ecological purification based on microalgae cultivation, comprises: (1) biogas slurry pretreatment; (2) habituated culture of autotrophic microalgae, namely, obtaining algae strains capable of rapidly growing in 70-100% biogas slurry; (3) preparation of a seed solution; (4) a biogas slurry purification method during growing of microalgae, namely, after expanded cultivation, inoculating the habituated algae species into an open photobioreactor for cultivation, obtaining Chlorella biomass growing by high density through a semi-continuous culture method and optimized methods such as fed-batch cultivation, and purifying the biogas slurry; (5) biochemical breaking of microalgae cell walls, namely, introducing the microalgae cells into a biochemical wall breaking pool, putting freshwater fish into the pool, and obtaining algae slurry subjected to wall breaking; and (6) collection of the microalgae cells and recycling of the biogas slurry.
NOVELTY - A CeDGATl protein comprising 713 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The CeDGATl protein is useful for producing yeast cell, plant or algae with high fatty acid content including palmitic acid, palmitoleic acid, stearic acid and/or oleic acid content and biodiesel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) gene encoding the above-mentioned CeDGATl protein; (2) vector comprising the above-mentioned gene; (3) host cell comprising the above-mentioned protein, gene, or vector; and (4) method for producing yeast cell, plant or algae with high fatty acid content including palmitic acid, palmitoleic acid, stearic acid and/or oleic acid content, involves introducing the above-mentioned gene in yeast cell, plant or algae, where the yeast includes Saccharomyces cerevisiae, the algae is Chlorella, and the plant includes Arabidopsis thaliana, tobacco, rape, sunflower, soybean, Solanum lycopersicum, castor, cotton, sesame or peanut.
NOVELTY - A kind of solar energy straw wet oxidation process producing marsh gas device, especially a solar power supply device, and a device for generating hydrogen by stage fermentation marsh gas and straw wet oxidation treatment process. It is the device to external device and solar energy power supply, the power supply is connected with the solar device, apparatus is provided with clapboard, one side of the upper part of the pre-processing device, a pre-processing device is a feeding port, a lower part is wet-oxygen device, discharging device on the lower part of the rotating shaft and the device is a fermentation device, the inner part is a stirring device, the stirring device is connected with the upper end and the lower end of the rotating shaft is set with a stirring paddle, the middle part is set with separating plate, rotating shaft of the stirring device passes through the separating plate. The time for fermentation of straw and processing device wet oxidation treatment by the wet oxidation pre-processing device, and pre-processing the stirring device can stir for fermentation, fermentation is separating plate at the lower part to prevent fermenting steam exploded wood fibre straw is not completely, improving the fermenting steam exploded wood fibre straw.
NOVELTY - This utility model claims a kind of used for purifying sewage of the space filler, comprising two connecting belts, two connecting belts is provided with fabric adsorption strips of a plurality of plane between the adjacent fabric adsorption strips at intervals with a certain distance. The fabric adsorption strips single surface is provided with an adsorption loop to form a single surface absorption loop structure or fabric adsorption strips of plane is a double-layer structure, the two sides are provided with an adsorption loop to form double-surface absorption loop structure. This utility model is a plane structure, it is very convenient, it is convenient to install, saves manufacturing time of filling bracket. This utility model imitates a b shape, light weight, low cost, convenient maintenance, long service life. This utility model has large specific surface area, quick film hanging speed, and it is not easy to hidden nano sludge. This utility model is suitable for wide application range, a ten cubic small landscape water pool to more than one hundred millian lake cubic all can be used.
NOVELTY - Preparing pesticide comprises extracting Croton, chaulmoogra, nux vomica and liposome, crushing into powder of 40 meshes, adding wheat bran and 75% times of water, uniformly stirring, sterilizing for 20 minutes, inoculating 3.342% of Trichoderma viride and 0.3-1% of Aspergillus niger, keeping the temperature to 20-25 degrees C, culturing for 48-72 hours, adding 3000 pts. wt. of water, keeping the temperature at 40-45 degrees C for 48-72 hours, hot reflux extracting at 40-45 degrees C for 1-2 hours, mixing two liquids, vacuum decompressing, concentrating to 60 degrees C, and filtering.    USE - The pesticide is useful for plant.    ADVANTAGE - The pesticide is prepared with high quality, rich resource and inexpensive, and environment-friendly.
NOVELTY - A kind of town polluted surface water purifying device, wherein the device comprises a suspension device, tank, oxygen increasing pump, oxygen aeration device, blower, target dispenser and a power supply system, can provide power to the urban polluted water purifying device is provided with a suspension device, the air outlet of the oxygen increasing pump is provided with a strain in the tank, tank and aeration device is connected with one end of the air pipe is connected with the oxygen increasing aeration device connected with the other end of the air guide pipe, and the target dispenser and oxygen aeration device are connected with each other. A. the mycelium cultivation technology, high efficiency oxygenation technology and targeting adding a connection with the more simple operation than the prior art, and the effect is quick.
NOVELTY - This utility model claims a kind of using mature stage after the corn straw high-efficiency producing volatile fatty acid by anaerobic fermentation marsh gas, comprising a silage fermentation tank (1), a homogenizing tank (4), a hydrolysis acidification tank (8) and anaerobic fermentation tank (11), silage fermentation tank (1) by the conveyor belt (3) is connected with the slurry tank (4), slurry tank (4) through conveying pipeline (19) and the hydrolysis acidification pool (8), the hydrolysis acidification pond (8) through the B delivery pipe (20) and the anaerobic fermentation tank (11). This utility model is capable of using corn straw for mature stage after producing marsh gas by using silage fermentation tank, a homogenizing tank, a hydrolytic acidification tank and anaerobic fermentation. In addition, it can ensure the use safety of the device is provided with a high and low pressure protector in the anaerobic fermentation tank to prevent the explosion and makes up the deficiency of the existing technology.
NOVELTY - A kind of anaerobic-aerobic alternate particle sludge sewage treatment device, belonging to the field of sewage treatment technology, the bottom of the tank body is provided with a water inlet pipe and an air inlet pipe, the inner wall of the tank body is provided with a water distribution pipe and a water inlet pipe connected to the upper side of the water distribution pipe is provided with micro-pore aerator is connected with air inlet pipe, the outer side of the upper end of the tank body is provided with weir through the return pipe and a water inlet pipe connected with a water outlet pipe is connected with the water tank, the top of the tank body is set with three-phase separating device, the top of the three-phase separating device is provided with an air outlet, the lower part of the tank body is set with three-phase separating device guide plate, the tank body is provided with a gas collecting pipe, a guide plate, the air outlet is connected with a separating device is connected with the gas collecting tube. This utility model has advantages of capable of fast forming granular sludge in the sewage to remove most organic pollutant and improve the biodegradability, generating marsh gas can be used as the energy utilization, anti-impact load ability is strong, it can save area and improve the processing efficiency and reduce processing cost and cost.
NOVELTY - The utility model claims a domestic sewage disposing a biochemical culture bag, comprising bag opening is provided with a double layer bag, the bag from inside to outside in turn is culture bag and vacuum bag, wherein the culture bag and vacuum bag is provided with vacuum bag for supporting the bracket. This utility model is made of a biodegradable material, a culture bag for the vacuum bag support frame supporting a control of domestic sewage biochemical culture medium material of edible fungus concentration, temperature and so on, it not only saves medicine, but also effectively shortens the culture time, improve the developing efficiency and convenient operation. This utility model is simple in structure, low in cost, using the inherent key can be a biochemical bacteria culture to the food supplement, bag mouth sealing can be placed in any position to the domestic sewage treatment system, which can bring good economic benefit for the enterprise.
NOVELTY - This utility model claims a kind of marsh gas generating bag, belonging to the technical field of marsh gas. It solves the problem that the existing technology of marsh gas generating device has complex structure, high production cost and so on. The marsh gas generating bag, comprising a bag opening of the bag body, the bag body is provided with a straw containing a storage cavity, wherein the inner wall of the bag opening to seal the bag mouth of the sealing strip and the sealing strip, the sealing strip and the sealing strip II are matched with the bag body is further provided with a storage cavity is connected with the through hole, the through hole is provided with an air outlet valve. This utility model has simple structure and low production cost.
NOVELTY - Preparing organophosphate pesticide chlorpyrifos treatment agent involves: directly putting 20-125 mu M tea extract epigallocatechin gallate (EGCG) into organophosphorus pesticide chlorpyrifos-containing wastewater i.e sewage, adjusting pH 4.6-7 at water temperature of 20-30 degrees C; irradiating the waste water mixture with high pressure mercury lamp light at 125-150 W for 10-12 minutes; adding complexing agent to water in high pressure mercury lamp at same concentration as the added tea extract EGCG, to precipitate and filtering.    USE - For preparation of organophosphate pesticide chlorpyrifos treatment agent (claimed); in drinking water, polluted underground water in remote areas, and for treatment of irrigation water.    ADVANTAGE - The method is natural and uses environment friendly treating agent and the dosage is little, convenient use and operation, has low running cost, high efficiency and no environment pollution and is suitable for wide application range, do not affect the operation of the system, the change of the environment condition, do not need special production process directly, and the human body such as, use the light having a wavelength greater than a processing time to save energy.    DETAILED DESCRIPTION - Preparation of organophosphate pesticide chlorpyrifos treatment agent involves: directly putting 20-125 mu M tea extract epigallocatechin gallate (EGCG) into organophosphorus pesticide chlorpyrifos-containing wastewater i.e sewage, adjusting to pH 4.6-7 at water temperature of 20-30 degrees C; irradiating the waste water mixture with high pressure mercury lamp light at 125-150 W for irradiation time of 10-12 minutes; adding complexing agent to the water in high pressure mercury lamp, at same concentration as the added tea extract EGCG, to precipitate and filtering to remove organophosphate pesticide chlorpyrifos. The complexing agent is Al3+, Zn2+ or Fe3+.
NOVELTY - The utility model claims one method for restaurant and kitchen rubbish processing system, belonging to the waste processing technology field. Said of the kitchen garbage processing system, comprising a kitchen garbage storage bin, kitchen garbage storage bin and a crusher, beater, a hydrothermal reactor, an anaerobic reaction tank, a filter press, a biogas residue tank, biomass fuel rod forming machine, in turn connecting, orderly connecting the biogas liquid tank and sewage processing pool. The anaerobic reaction tank and the marsh gas tank, marsh gas purifying device are connected in turn. The utility model low carbon, environment-friendly, safe and reliable, high degree of resource, low energy consumption, reduce the increasingly increased ambient pressure, for the society saves huge resource.
NOVELTY - This utility model claims one kind of natural heating type organic waste processing device and processing method of organic waste, naturally heating type organic waste processing device with fermenting in the fermentation tank is provided with a stirring device, stirring the operation frequency of the device is as follows: the feeding time tank stirring device initial operation one time binary two back stirring, stirring device initial operation one time binary two back stirring over the said stirring device each for 6 + 0.5 operation one time binary two reverse turning until the fermentation under stirring one time. Organic mixture through a certain time after stirring device moving to the discharging port of the fermentation tank to form primary organic fertilizer. The utility model of the whole fermentation process does not need other energy consumption, it does not need electricity or natural gas heating, which not only can convenient and effective processing organic waste, but also saves energy.
NOVELTY - This utility model claims one kind of DNA production device. Said DM production device, comprising a reactor, a reactor with feeder, feeder ammonia water, sodium hypochlorite feeder is connected with reactor is connected with the active carbon adsorption tank, filter, and dryer are connected in turn, respectively connecting filter active carbon filter, a vacuum pump, an active carbon filter and active carbon recovery tank, a vacuum pump, a waste liquid tank are respectively connected with the waste liquid tank is connected with the reactor. The utility model has simple operation, good effect, saves the raw material, the whole device without waste liquid discharge and protects the environment.    USE - The device is useful for preparing dextromethorphan (claimed).    ADVANTAGE - The device is simple to operate, and effectively prepares the dextromethorphan with reduced amount of raw materials and without discharging the waste liquid.
NOVELTY - This utility model claims one kind of domestic biomass gasification furnace, belonging to the waste material in the agricultural production into the gasification device technical field of combustible gas, which is aimed to provide one effective and practical domestic biomass gasification furnace. The utility model comprises a fan, an air inlet pipe, the gasification furnace, a filter, an exhaust switch, an exhaust pipe, a gas storage tank, a gas stove, air distribution switch and tar discharging switch, said fan is connected with the air inlet pipe, connecting, connecting gasification generation furnace air inlet pipe and filter, the filter connecting exhaust switch, an exhaust pipe and an air storage tank, air storage tank and gas stove, air distribution switch and tar discharging switch connecting. The utility model is the biomass through the enclosed anoxic, the destructive distillation pyrolysis and produce mixed combustible gas of one high-efficiency energy-saving biomass gasification furnace can be applied to all kinds of biomass-resource-gasification, the gas can be used for single user cooking and warming.
NOVELTY - The utility model claims one anti-combustion type double-medium domestic garbage gasification furnace, comprising a furnace body, an upper furnace body has a furnace cover, an air inlet, a steam inlet, a electric lighting device, water inlet, ash outlet, gas outlet, water outlet, a heat insulating layer, a furnace body from up to down in turn is dry layer, hot de-layer, an oxide layer, a reducing layer, an ash is one kind of new-type household garbage processing device to realize the harmlessness, reduction and resource;
NOVELTY - The utility model claims one aerobic fermentation device, comprising at least one fermentation, fermentation is composed of three wall body and one surface without the wall, the height 200 cm, and the width is 100 to 300 cm, the length is at least 300 cm, outside the wall foot of the wall body of the drain hole 100 cm one of the drain hole is connected to the one of the outer ditch aerobic fermentation device, is equipped with at least one group of aeration pipe, one of the aerobic fermentation device without wall is provided with one plug. The utility model not only is suitable for small farm, is more suitable for large scale farm cycle operation and industrialization continuous production, fermentation speed is fast and the quality is good. aerobic fermentation not only solves the pollution problem, agricultural production and the nuisanceless cultivation base material or fertilizer, improves the overall performance.
NOVELTY - Streptomyces lavendulae strain having preservation number of CGMCC No.7548, is new.    USE - The Streptomyces lavendulae strain is useful in: the preparation of seaweed microbial fertilizer by using seaweed slag, and microbial fertilizer antagonism of Rhizoctonia solani, Fusarium oxysporum, Fusarium solani, Fusarium moniliforme, apple black rot Diaporthales, wheat root rot pathogenic fungi, corn small spot disease, and anthrax bacteria (all claimed).    ADVANTAGE - The strain has good degradation effect of seaweed; can not only extract sodium alginate from seaweed while processing industrial waste residues but also can be re-utilize sodium alginate; produces antibiotic active substances having good metabolic activity during the fermentation process which can effectively inhibit the growth of various pathogenic microorganisms; has good production yield, and good growth-promoting effect; and is suitable for agricultural production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of Streptomyces lavendulae strain in the preparation of seaweed microbial fertilizer by using seaweed slag.
NOVELTY - A biofertilizer comprises 50-60 wt.% humic acid, 15-20 wt.% charcoal and 10 wt.% binder, prepared by fermenting sludge at 30-45 degrees C with water content of 35-45 vol.% at pH 5.5-8, adding humic acid, charcoal and adhesive, stirring, crushing, granulating until humidity reaches 40%, pelletizing with particle diameter of 2.5-4 mm, drying formed particles in drying machine through conveyor belt with dryer inlet at 80 degrees C and outlet temperature of 600 degrees C, air cooling via fan blowing, sieving according to specification, metering, packaging and storing.    USE - Sludge biofertilizer.    ADVANTAGE - The fertilizer is environment-friendly.
NOVELTY - An alcohol-based fuel comprises 42500-45000 pts. wt. methanol, 5 pts. wt. acetone, 0.012 pts. wt. potassium permanganate, 0.3 pts. wt. hydrogen peroxide, 0.5 pts. wt. copper sulfate, 0.003 pts. wt. camphor oil and 2500-5000 pts. wt. water.    USE - Alcohol-based fuel (claimed).    ADVANTAGE - The alcohol-based fuel is economical and environmentally-friendly and has excellent combustion effect.
NOVELTY - A co-solvent comprises 20-60 volume% biodiesel, 35-65 volume% carbon alcohol and 5-15 volume% emulsifier.    USE - Co-solvent is used for improving storage stability of ethanol diesel (claimed).    ADVANTAGE - The ethanol diesel provided using co-solvent has excellent storage stability and water resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ethanol diesel oil, which comprises diesel oil, ethanol and co-solvent.
NOVELTY - This utility model claims one kind of biochemical sludge processing device, belonging to the waste processing technology field. Said biochemical sludge processing device, comprising a biochemical sludge storage bin, biochemical sludge storage bin and the feeder, a pre-heater, a hydro-thermal reactor, one-stage anaerobic reaction tank, two-stage anaerobic reaction tank, a filter press, a biogas residue tank, biomass fuel rod forming machine, in turn connecting, orderly connecting the biogas liquid tank and sewage processing tank, one-stage anaerobic reaction tank, two-stage anaerobic reaction tank are respectively connecting marsh gas tank, marsh gas tank connecting biogas purifying device. The utility model has high resource and energy consumption is low, and it is safe and reliable, reducing the increasingly increased ambient pressure, for the society saves huge resource.
NOVELTY - This utility model claims one kind of biochemical sludge processing system, belonging to the waste processing technology field. Said biochemical sludge processing system, comprising a biochemical sludge storage bin, biochemical sludge storage bin and the feeder, a pre-heater, a hydro-thermal reactor, an anaerobic reaction tank, a filter press, a biogas residue tank, biomass fuel rod forming machine, in turn connecting, orderly connecting the biogas liquid tank and sewage processing pool, an anaerobic reaction tank orderly connecting marsh gas tank, marsh gas purifying device, hydro-thermal reactor is connected in series. The utility model is safe and reliable, high degree of resource, low energy consumption, reduce the increasingly increased ambient pressure, for the society saves huge resource.    USE - The system is useful for processing a biochemical sludge.    ADVANTAGE - The system processes the biochemical sludge in a safe and reliable manner with less energy consumption, and with reduced ambient pressure.    DETAILED DESCRIPTION - The biochemical sludge processing system comprises a biochemical sludge storage bin connected with a feeder, a pre-heater, two hydro-thermal reactors, an anaerobic reaction tank, a filter press, a slag slot, a biomass fuel rod forming machine, and a boiler, where the hydro-thermal reactors are a single level hydro-thermal reactor and two level hydro-thermal reactor that are connected in series. The filter press is connected with a biogas liquid tank and a sewage processing tank. The anaerobic reaction tank is connected with marsh gas tank and a methane purifying device. The boiler is connected with the hydro-thermal reactor. The slag slot is connected with an organic compound fertilizer synthesis tank. The biochemical sludge storage bin is connected with the feeder using a feeding screw.
NOVELTY - The utility model belongs to kitchen waste processing field, specifically relates to one kind of biomass fuel rod forming device. The utility model claims biomass fuel bar forming device, comprising connecting the biogas slag groove, machine, screening chamber, a drier and the lower, the lower material chamber is provided with a first conveyor belt, a first belt connecting fuel rod forming machine of upper part and lower fuel rod forming machine part with a discharging port, the fuel rod forming machine is set below the second conveyor belt, upper second conveyor belt with a material tank. The second conveying belt with the automatic packing machine. One side of the second conveying belt cutter, upper cutter with a scraper. The utility model claims biogas residue to kitchen waste processing as raw material, and sieving to make the fuel stick forming machine abrasion is reduced to minimum, preparing to obtain the fuel can replace conventional petrochemical energy, and has no pollution, the kitchen garbage can be fully used, the cost is low and it is environment-friendly.    USE - The device is useful for forming biomass fuel rod (claimed).    ADVANTAGE - The device economically forms the biomass fuel rods in an environmentally friendly manner.
NOVELTY - Rhodium-based catalyst comprises active component, additive and carrier. The active component is rhodium, additive is manganese oxide, and carrier is carboxylated carbon nanotubes. The content of rhodium is 1-15 wt.%. The mass ratio of rhodium and manganese is 0.5-20.    USE - Rhodium-based catalyst used for synthesizing ethanol and co-producing methane.    ADVANTAGE - The rhodium-based catalyst has improved catalytic activity, and provides alcohol with high yield. Methane obtained using the rhodium-based catalyst has high selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the rhodium-based catalyst. Rhodium nitrate (Rh(NO3)2) solution and manganese nitrate (Mn(NO3)2) solution are dissolved in an alcohol solvent, to obtain a mixed solution. The carboxylated carbon nanotubes are added to the resultant mixed solution, stirred until uniformly dispersed, heated and further stirred until the solvent evaporates completely, dried, roasted and reduced, to obtain rhodium-based catalyst.
NOVELTY - An active catalyst component precursor, auxiliary agent precursor and catalyst carrier are mixed, combustion agent and dispersing agent are mixed, ball-milled for 20-60 minutes. The ball-milled materials are added to crucible or quartz placed in muffle furnace at 300-600 degrees C for 30-60 minutes, to obtain catalyst. The active catalyst component precursor is nickel nitrate. The catalyst carrier precursor is aluminum nitrate or pseudoboehmite. The catalyst carrier is aluminum oxide. The combustion agent is urea.    USE - Preparation of urea combustion method methanation catalyst (claimed).    ADVANTAGE - The method provides methanation catalyst within a short period of time, by a simple process.    DETAILED DESCRIPTION - An active catalyst component precursor, auxiliary agent precursor and catalyst carrier are mixed, combustion agent and dispersing agent are mixed, ball-milled for 20-60 minutes. The ball-milled materials are added to crucible or quartz placed in muffle furnace at 300-600 degrees C for 30-60 minutes, to obtain catalyst. The active catalyst component precursor is nickel nitrate. The content of active catalyst component precursor is 5-55 wt.% with respect to total weight of catalyst. The auxiliary agent is oxides of cerium, calcium, cobalt, lanthanum, zirconium, samarium, barium, manganese, iron, molybdenum, titanium or copper. The catalyst carrier precursor is aluminum nitrate or pseudoboehmite. The catalyst carrier is aluminum oxide. The combustion agent is urea.
NOVELTY - Arc discharge plasma decomposition of water into hydrogen involves providing water evaporation chamber and catalytic chamber comprising catalyst particles containing nickel and manganese ferrite particles, heating liquid to vapor state, performing catalytic cracking, and decomposing water molecule into oxygen gas molecules and hydrogen molecules. The plasma decomposition method is implemented in hydrogen production system.    USE - Arc discharge plasma decomposition of water used in hydrogen production system.    DETAILED DESCRIPTION - Arc discharge plasma decomposition of water into hydrogen involves providing water evaporation chamber and catalytic chamber comprising catalyst particles containing nickel and manganese ferrite particles, heating liquid to vapor state, performing catalytic cracking, and decomposing water molecule into oxygen gas molecules and hydrogen molecules. The plasma decomposition method is implemented in hydrogen production system having water tank, control unit, water evaporation catalytic converter, temperature sensor, central processing unit, high frequency high voltage power supply and temperature sensor.
NOVELTY - The system has main reaction furnace (1) which is provided with feeding port and discharging port and connected with heating cavity connected with first medium inlet and first medium outlet. The main reaction furnace and secondary reacting furnace (2) are connected with nitric oxide supply device (3). The water vapor supply device of main reaction furnace is connected with hydrogen producing device (5). The discharge hole of main reaction furnace is set with hydrogen separation device (6) connected with inlet of the hydrogen storage device.    USE - Totally-enclosed thermo-chemical hydrogen production system for power supply device (claimed).    ADVANTAGE - The closed loop continuous hydrogen production lines can be formed under the combined effect of amorphous metal catalyst and by-products can be recycled. The waste discharge can be avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a power supply device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the totally-enclosed thermo-chemical hydrogen production system. (Drawing includes non-English language text)    Main reaction furnace (1)    Secondary reacting furnace (2)    Nitric oxide supply device (3)    Hydrogen producing device (5)    Hydrogen separation device (6)
NOVELTY - Cultivating material of Stropharia rugosoannulata, comprises 54-64 wt.% white pepper sheath leaf, 12-22 wt.% bran, 10 wt.% vegetable garden soil, 10 wt.% lime powder and 2 wt.% gypsum powder.    USE - Cultivating material of S.rugosoannulata.    ADVANTAGE - The cultivation material can be easily absorbed by the mycelium as it contains simple substance, promotes growth and yield of the mycelium, and has biological efficiency of 105.6-118.2%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing S.rugosoannulata culturing material, which involves soaking bamboo sheath leaves in water and then in lime water for 30-36 hours, obtaining wastewater, removing truss, directly piling, paving a layer of white pepper leaf sheath and then a layer of rice husk and vegetable garden soil, sprinkling water, naturally fermenting the materials for 10-12 days, adding gypsum powder and bran, then adding water, stopping fermentation and maintaining the water content of the culture material is 63-65%.
NOVELTY - Usage method of circulating gas as fuel of carbon powder involves feeding dried wood chip into rigid feeding machine, pre-heating, passing obtained product into combustion chamber through injection device, performing high-temperature cracking, cooling, combusting, passing obtained gas to mist removal device and electric tar reactor, absorbing impurity anion and electronic electric field coulomb force by changing electric field time to precipitate, absorbing precipitate, purifying and passing optimized gas as fuel for combustion chamber.    USE - Usage method of circulating gas as fuel of carbon powder (claimed).    ADVANTAGE - The circulating gas is economically utilized as fuel of carbon powder by environmentally-friendly and simple method.    DETAILED DESCRIPTION - Usage method of circulating gas as fuel of carbon powder involves selecting wood chip, drying wood chip, such that water content is 15%, feeding dried wood chip into rigid feeding machine, then passing the rigid feeding machine to pre-heating device, pre-heating for 3-5 minutes, passing obtained product in pre-heating device into combustion chamber through injection device, performing high-temperature cracking, passing obtained material into cooling twisting cage, cooling to 300-400 degrees C to obtain carbon powder, performing combustion process to produce gas containing oil mist, passing the gas through fuel gas pipe to mist removal device, passing obtained gas into electric tar reactor when gas contains reduced tar and impurities, absorbing impurity anion and electronic electric field coulomb force by changing electric field time to precipitate after releasing charged electrode, absorbing precipitate on electrode, purifying, then passing purified gas through gas pipe to electrostatic dust remover, and passing optimized gas as fuel for combustion chamber.
NOVELTY - Carbon fixation method of municipal sludge and crop straw involves crushing dry crop straw to a length of less than 50 mm, adding the sludge to the water under moisture content of less than 25%, then crushing, mixing mixture of straw and mud into charcoal furnace, heat generating under anaerobic conditions biochar, reacting at 400-500 degrees C, non-continuous heating to the reaction gases, stopping heating, cooling and removing the material. The weight ratio of crushed sludge and dry straw is 1-3:1-3.    USE - Carbon fixation method of municipal sludge and crop straw (claimed).    ADVANTAGE - The carbon fixation method of municipal sludge and crop straw having excellent stability, and high collecting efficiency, is economically enabled, by a simple method.
NOVELTY - A carbonized cobalt material comprises cobalt carbide binary alloy and lanthanum-magnesium-nickel-based alloy composite.    USE - Carbonized cobalt material is used for hydrogen-storage electrode for battery (all claimed).    ADVANTAGE - The battery containing the carbonized cobalt material has excellent cycle characteristics, corrosion resistance, discharge capacity and power characteristics. The carbonized cobalt material is capable of reversibly absorbing and releasing hydrogen at normal temperature and normal pressure.    DETAILED DESCRIPTION - A carbonized cobalt material comprises cobalt carbide (CoCx, where x is 1, 2 or 3) binary alloy and lanthanum-magnesium-nickel-based alloy composite. INDEPENDENT CLAIMS are included for the following:    (1) hydrogen-storage electrode, which has nickel powder and carbonized cobalt material as hydrogen storage material; and    (2) preparation of carbonized cobalt material.
NOVELTY - The system has a liquid ammonia storage tank (1) to store the liquid ammonia (5) that is transferred to an active material storage tank (4) through an ammonia charging pipe (6). A filter (2) and a stainless steel switch valve (3) are fixed in the ammonia charging pipe. The ammonia is entered into next active material storage tank according to the effect of a gas circulating pump (11). The active material storage tanks are connected in series by the ammonia charging pipe for charging the ammonia. The filter is filled with zeolite and industrial anhydrous calcium oxide powder.    USE - Solid ammonia circulation system for selective catalytic reduction (SCR) of automobile tail gas processing system and fuel cell electric vehicle (FCEV).    ADVANTAGE - Multiple ammonia-storing tanks are connected in series or in parallel, thus the efficiency of system can be improved. The leakage of ammonia in production environment can be reduced. The safety and reliability of the system can be improved, and the system can be manufactured at low cost. The system can be maintained easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid circulation system.    Liquid ammonia storage tank (1)    Filter (2)    Stainless steel switch valve (3)    Active material storage tank (4)    Liquid ammonia (5)    Ammonia charging pipe (6)    Gas circulating pump (11)
NOVELTY - The fuel cell system includes a fuel cell portion (2) that produces electric power from reaction between oxidizing gas containing oxygen and fuel gas supplied from a fuel generating member (1). An electric circuit (3) applies pulse current to the fuel cell portion, then measures the voltage between the fuel electrode (2B) and oxidizing agent electrode (2C) of the fuel cell portion during the pulse current application. The electric circuit then detects the oxidation state of the fuel generating member based on the measured voltage.    USE - Fuel cell system.    ADVANTAGE - Negates need for a large-scale apparatus to detect the oxidation state of the fuel generating member. Ensures precise detection of the oxidation state of the fuel generating member using the voltage of the fuel cell portion during pulse current application.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the fuel cell system. (Drawing includes non-English language text).    Fuel generating member (1)    Fuel cell portion (2)    Fuel electrode (2B)    Oxidizing agent electrode (2C)    Electric circuit (3)
NOVELTY - The device (100) has a cutter (80) which manufactures the fuel cell stack part and in which a gas diffusion layer (3) is equipped in both sides of a membrane-electrode assembly. The cutter is installed at a frame (10) that is movable by a drive unit (40). The frame is installed in an upper die. A lower die fixes a membrane-electrode assembly base material (7) and gas diffusion layer in the lower side of the upper die. A junction unit (70) is provided that comprises a hot plate (71) which is compressed to both sides of the membrane-electrode assembly base material and the gas diffusion layer.    USE - Device for manufacturing fuel cell stack.    ADVANTAGE - The device has a cutter which manufactures the fuel cell stack part and in which a gas diffusion layer is equipped in both sides of a membrane- electrode assembly, where the cutter is installed at a frame that is movable by a drive unit, and hence ensures an improved fuel cell stack manufacturing device with which the damage and inferiority rate of the bonded part and the cycle time are reduced.    DETAILED DESCRIPTION - The drive unit includes a gear group (65) that decelerates the rotation power of the motor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a fuel cell stack manufacturing apparatus.    Gas diffusion layer (3)    Membrane-electrode assembly base material (7)    Frame (10)    Drive unit (40)    Gear group (65)    Junction unit (70)    Hot plate (71)    Cutter (80)    Fuel cell stack manufacturing apparatus (100)
NOVELTY - This utility model claims one kind of vegetable greenhouse for fermentation device, comprising a base, a bracket and a supporting rod, said base is square hollow structure, said base is provided with a vent hole, said fence bracket is composed of bearing bar's at least six parallel, adjacent said bearing's distance between the same, said fence bracket are set at two sides of one operation rod, the operation rod and the said each one of bearing fixing connecting rod, said base is vertically set up at least four supporting rod, four supporting rod is set one ring woven plastic cloth to form one cylindrical container, said woven plastic fabric lining a layer of plastic thin film. The utility model's beneficial effects are, the utility model has reasonable structure, the wet straw with fresh excrement after uniformly stirring, and then added into the cylindrical container's product, taking the fermentation is improved by CO2 concentration in the greenhouse's vent's's is set under it's fermentation efficiency is improved, and energy-saving and environment-friendly, green and pollution-free, and it has wide market prospect.
NOVELTY - Vegetable leaf waste organic fertilizer quantitative material dispensing machine, the machine of vegetable leaf quantitative device, quantitative device, a conveying belt and a mixing cylinder, leaf quantitative device composed of a main bracket, a main hopper, a feeding belt and first dynamic weighing belt, a discharge port's main hopper is equipped with discharging claw's shaft, a discharging device by secondary bracket, assistant ingredient hopper, a spiral conveying pipe and second dynamic weighing belt is set with an elastic shaft, a discharge port's claw with elastic material is equipped with upper flashboard connecting with the cylinder, is provided with upper , stirring roller is provided with spiral mixing cylinder's arc-shaped blades are arranged in the discharge port's side. Time using, the material are transmitted to a leaf quantitative device and device in the ingredient's amount of material by a dynamic weighing belt in the conveying process to it's upper material weighing, taking weight signal feedback control, the dynamic weighing belt's material output's metering accurately and uniformly stirring the material in the mixing cylinder to form a quantitative ratio's organic fertilizer raw material.
NOVELTY - The utility model claims one for organic fertilizer fermenting's charging device, comprising a charging pipe, a handle pipe, an air compressor, a control device, with the handle tube, and the other end of the handle tube's through the pipeline connecting with the air compressor, the air compressor and the control device connected with the upper air tube is provided with multiple air charging hole, the aperture's charging hole is 0.5-1.5 mm, and the length's inflation tube is 2-4 m, the diameter's inflation tube is 7-10 mm. The utility model's beneficial effects as organic fertilizer using this utility model saves the step's greenhouse in the stacking fermentation process, reduces the cost, but also the fermentation time is short, the period and compared with the previous five days, the working efficiency is improved one time; the utility model has charging device, organic fertilizer fermenting fully, high content of organic matter, which is good for growing's crops, has simple structure, is easy to manufacture, high working efficiency, low cost and long service life and so on.
NOVELTY - Biomass fuel is combusted by drying biomass, crushing into powder with fineness of less than or equal to 20 mesh by crusher, and packing.    USE - Biomass fuel combustion method (claimed).    ADVANTAGE - Large-scale production of biomass fuel can be achieved, air pollution can be reduced, biomass fuel can be easily transported, and energy conversion rate can be improved. Biomass fuel can replace coal and other fuels.
NOVELTY - Livestock and poultry farms organic waste processor energy drain device comprises a suction port, an air suction electromagnetic valve (13), a blower (5), and a discharging pipe (12). A cyclone dust remover (3) with steam-water separator (4) pipeline is connected with the steam-water separator. An electric three-way valve (7) exhaust port through the return pipe (10) is set with horizontal U-shaped barrel (1) return port pipeline. An electric three-way valve (11) and a transverse liquid conveying pipe (8) are included.    USE - Livestock and poultry farms organic waste processor energy drain device.    ADVANTAGE - The device is energy saving, and has improved work efficiency.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the livestock and poultry farms organic waste processor energy drain device.    U-shaped barrel (1)    Cyclone dust remover (3)    Steam-water separator (4)    Blower (5)    Electric three-way valve (7)    Transverse liquid conveying pipe (8)    Return pipe (10)    Electric three-way valve (11)    Discharging pipe (12)    Air suction electromagnetic valve (13)
NOVELTY - Preparation of organic fertilizer comprises mixing 5-6 pts. wt. livestock excrement, 4-5 pts. wt. humic acid powder and 1-2 pts. wt. urea, adding biological strain, stirring for 10-20 minutes, crushing material after fermentation, evaporating, heating at 45-50 degrees C, granulating, sieving, and preparing into fertilizer.    USE - Method of preparation of organic fertilizer (claimed).
NOVELTY - Preparing green amifostine trihydrate involves using water solution, N-methyl-1,3-diamine, hydrogen acid salt and thio sodium phosphate at 10-70%, accelerating agent, and low carbon alcohol or polyol, the reaction temperature is 5-60 degrees C, directly filtering to obtain crude product of amifostine trihydrate, re-crystallizing and purifying for two times, to obtain medical amifostine trihydrate.    USE - The method is useful for preparing green amifostine trihydrate (claimed).    ADVANTAGE - In method for preparing amifostine, the quality is high, and there is no high boiling point solvent residue. The method is green and environment-friendly. It provides high efficiency, easy operation and low cost, and is suitable for industrial scale production.
NOVELTY - Preparing pharmaceutically acceptable amifostine trihydrate involves using water solution, N-methyl-1,3-diamine, hydrogen acid salt, thio sodium phosphate at 10-70%, and N,N-dimethyl acetamide as promoter, the reaction temperature is 5-60 degrees C, directly filtering to obtain crude product of amifostine trihydrate, and re-crystallizing and purifying for two times, to obtain medical amifostine trihydrate.    USE - The method is useful for preparing pharmaceutically acceptable amifostine trihydrate (claimed).    ADVANTAGE - The method is environment-friendly, low cost, and simple; and provides high efficiency, and convenient operation; and is suitable for industrial scale production.
NOVELTY - Producing chicken manure organic fertilizer comprises uniformly mixing the padding material chicken, chicken and/or chicken excrement and zeolite to obtain the mixture; carrying out aerobic fermentation to the mixture for fully curing the excrement microbial inoculum, turning condition in a batch and taking aerobic fermentation microbial inoculum containing Aspergillus oryzae, Bacillus subtilis and yeast, stacking and aging the stacked fermented material.    USE - Method for producing chicken manure organic fertilizer (claimed).    ADVANTAGE - The method improves the quality of agricultural products, and improves the soil structure.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for producing chicken manure organic fertilizer (Drawing includes non-English language text).
NOVELTY - Manufacture of a plant growth promoting agent comprises livestock biogas anaerobic fermentation processing to increase liquid oxygen; filtering in an inorganic ceramic film membrane filter; carrying out nanofiltration membrane and reverse osmosis membrane concentration; and evaporating and concentrating.    USE - Method for the manufacture of a plant growth promoting agent used for crops and vegetables (claimed).    ADVANTAGE - The method is simple, safe and environment-friendly, and does not use synthetic chemicals.
NOVELTY - This utility model claims one kind of biogas residue high temperature aerobic fermentation composting device, comprising a biogas residue storage device, organic conditioning agent storage device, auxiliary storage device, mixing system, tower-type composting device device primary fermentation, secondary fermentation device and compost product storage device, the primary fermentation period is short (5d), low energy consumption (static process's 55.3%, drum-type dynamic process's 10%), small floor area, simple structure, comprising an inner tower and layering, discharging, and a ventilation radiating and multiple functions for improving's fermentation process condition is convenient operation and management and so on, it can reduce construction investment and operation cost, it can's residue after the anaerobic fermentation device for urban solid waste reduction, harmless and stabilized.
NOVELTY - Recycling solid containers, beverages or other liquids comprises: receiving a waste materials comprising at least one solid container and at least one liquid; separating the solid container from the liquid; concentrating sugars from the liquids to create feed stock; and generating bio-fuel from the feed stock.    USE - The method is useful for recycling solid containers, beverages or other liquids, where the container is plastic material, which is shredded, ground, washed or pelletized (all claimed).    ADVANTAGE - The method: reduces or eliminates discharge of waste materials; provides complete destruction and recycling of solids and related beverages and/or other liquids for reclamation; provides certification of destruction of submitted solids and liquids for generators; reduces or eliminates waste water loading to existing waste water treatment facilities; can purify water to higher industrial grades using a variety of filtration methods; utilizes immobilized microbe biological reactor technology to ferment and metabolize concentrated sugars and/or other materials; can produce ethanol, biobutanol, and/or acetone, and agricultural animal feed stock amendments, from mixed sugars and other waste materials; and can produce ultrapure bio-fuels/solvent products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for recycling solid containers, beverages or other liquids resulting in substantially no residual waste products comprising receiving waste materials comprising the solid container and the liquid, cutting the solid container, collecting the liquid from the container, recycling the solid container, concentrating sugars from the liquid to create feed stock, and generating bio-fuel from the feed stock.
NOVELTY - A solid high polymer type fuel cell system has MEA having fuel cell stack consists of laminated two or more single cells which produce electric power by using liquid organic compound as fuel. Through hole (107) is formed connecting the MEA and separator (103) laminated in at least one part of MEA. The through hole is separated from the flow path by the separator using a sealing material. The through hole is formed in space used as tank which stores liquid fuel or water.    USE - Solid high polymer type fuel cell system for using liquid organic compound as fuel when generating electrical power used when charging portable electronic devices. Uses include but are not limited to telephone, notebook computer, audio visual apparatus, camcorder and personal information terminal device.    ADVANTAGE - Offer reduction in cost by the reduction in number of components of solid high polymer type fuel system in which power density is improved by the compact structure of solid high polymer type fuel system.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the polymer electrolyte fuel cell in state omitted the upside current collecting plate and end plate.    Separator (103)    Through holes (105a,105b,106a,106b,107)    Current collecting plate (108)    End plate (109)
NOVELTY - Animals-and-plants residue is processed by passing oxygen-containing gas and carrying out aerobic fermentation of process target object (A) with deposited animals-and- plants residue, and aerated-fermentation process which adjusts airflow amount of oxygen-containing gas according to the inside temperature of process target object in 120-900 L/minute/m3 of process target object.    USE - Processing of animals-and-plants residue (claimed).    ADVANTAGE - Moisture content of animals-and-plants residue is reduced in a short time without using additional heat energy like a fossil fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing apparatus (1) of the animals-and- plants residue comprising accommodation installation (2) which accommodates process target object (A) which animals-and-plants residue deposits, gas flowing installation (3) which passes oxygen-containing gas in process target object, and temperature measurement installation (4) which measures the inside temperature of process target object.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing apparatus of animals-and-plants residue.    Processing apparatus (1)    Accommodation installation (2)    Bottom part (2a)    Side wall part (2b)    Leg part (2c)    Gas flowing installation (3)    Gas flowing part (3a)    Air blower (3b)    Gas volume adjustment part (3c)    Temperature measurement installation (4)    Process target object (A)
NOVELTY - The method involves carrying out denitrifying process of nitrogen-containing drainage biologically, when inflow of nitrogen-containing drainage natural water to denitrifying tank is stopped. One portion of to-be-processed water and activated sludge are circulated by system including denitrifying tank and aerator. The microorganism nutrient such as methanol of specific quantity is added corresponding to amount of nitrogen components of activated-sludge liquid mixture and amount of activated-sludge organic suspended solids of activated-sludge liquid mixture to denitrifying tank.    USE - Biological treatment method of nitrogen-containing drainage discharged from factory and office.    ADVANTAGE - The nitrogen load in natural water can be reduced, when there is no inflow of natural water, so that the reduction of the amount of activated sludge can be suppressed, thus the denitrifying process can be stably carried out at the time of resumption of process. The biological treatment method of nitrogen-containing drainage can be performed efficiently over long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biological treatment apparatus of nitrogen-containing drainage.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the relationship between nitrogen concentration in natural water tank and microorganism nutrient addition amount. (Drawing includes non-English language text)
NOVELTY - The method involves mixing sample gas with carrier gas i.e. helium gas, to make analysis gas, and measuring (S102) concentration before component total correction during analyzes of the analysis gas. A correction coefficient is calculated from a sum of component reference gas concentration and from a sum of concentration before component total correction, and the calculated correction coefficient is utilized. The concentration before component total correction in analyzes of the sample gas is corrected to make (S103) a concentration after component total correction.    USE - Gas-analysis method for measuring concentration of an isolated gas component to-be-measured.    ADVANTAGE - The concentration before component total correction in analyzes of the sample gas is corrected to make the concentration after component total correction, so as to obtain small difference at the time of total correction implementation and to obtain small repeatability of an emitted-heat amount value when measuring the emitted-heat amount value of natural gas, thus improving measurement performance of the emitted heat amount value.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a characteristic processing operation of a CPU performed in a gas chromatograph. '(Drawing includes non-English language text)'    Component reference gas concentration measuring step (S101)    Concentration before component total correction measuring step (S102)    Concentration after component total correction step (S103)
NOVELTY - Processing waste sludge using waste oil, comprises (a) supplying high temperature heated waste oil to waste sludge fryer by heating waste oil provided by waste oil repository, (b) splashing high temperature heated waste oil on the waste fiber and/or waste sludge in the fryer, (c) supplying the splashed waste fiber and the waste sludge to a de-oiling and drying machine and transferring the crystallized dye and water obtained in the step (b) to a separation tank, (d) de-oiling and drying and molding the de-oiled and dried waste fiber and waste sludge in a pellet molding machine.    USE - The method is useful in processing waste sludge using waste oil for manufacturing bio-coal (claimed).    ADVANTAGE - The method utilizes waste oil and thus it reduces environmental pollution, and separates water content and organic compound in the sludge by utilizing the high-temperature waste oil and discharges crystallized salt via evaporation and condensation.    DETAILED DESCRIPTION - Processing waste sludge using waste oil, comprises (a) supplying high temperature heated waste oil to waste sludge fryer by heating the waste oil provided by a waste oil repository through a heater to high temperature, (b) splashing the high temperature heated waste oil in the fryer on waste fiber and/or waste sludge provided by a waste fiber repository and a waste sludge repository, (c) supplying the splashed waste fiber and the waste sludge to a de-oiling and drying machine and transferring the crystallized dye and water obtained in the step (b) to a separation tank, (d) de-oiling and drying the splashed waste fiber and the waste sludge in the drying machine and molding the de-oiled and dried waste fiber and waste sludge in a pellet molding machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for processing waste sludge using waste oil for manufacturing bio-coal (Drawing includes non-English language text).
NOVELTY - An oxygen-permeable film (10) comprises mixture of stabilized zirconia as oxygen ion conductor and an electron conductor containing lanthanum-chromium-containing complex oxide (I). The oxygen-permeable film permeates oxygen from high oxygen partial pressure side to low oxygen partial pressure side, using oxygen partial pressure difference as drive force.    USE - Oxygen-permeable film (claimed) used for permeating oxygen used for generating hydrogen for fuel cell.    ADVANTAGE - The oxygen-permeable film has excellent oxygen-permeating performance.    DETAILED DESCRIPTION - An oxygen-permeable film comprises mixture of stabilized zirconia as oxygen ion conductor and an electron conductor containing lanthanum-chromium-containing complex oxide of formula: La1-xMxCrO3-z (I). The oxygen-permeable film permeates oxygen from high oxygen partial pressure side to low oxygen partial pressure side, using oxygen partial pressure difference as drive force.    M=element chosen from alkali-earth metals excluding magnesium;and    x=0-0.3.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of oxygen-permeating film and reformer.    Oxygen-permeating film (10)    Reforming raw material flow path (16)    Air flow path (18)    Modifier (20)
NOVELTY - Method for utilizing adhesive microalgae as biomass, involves inoculating the adhesive microalgae in an vertically installing a attachment medium, culturing by lifting and drying to obtain biomass.    USE - The method is useful for utilizing adhesive microalgae for readily converting adhesive microalgae contained in sewage or wastewater into biomass (claimed).    ADVANTAGE - The method exhibits high efficiency, is performed cost-effective, and simply and rapidly harvests the microalgae without other processes.
NOVELTY - Device for processing organic feedstock, comprises system of supply of initial feedstock, anaerobic bioreactor, biomass heater, biogas withdrawal system, biomass removing system, and technological process control system, where supply system of initial feedstock mechanism for disintegrating and mixing initial feedstock with initial feedstock heating system is included.    USE - The device is useful for processing organic feedstock (claimed).    DETAILED DESCRIPTION - Device for processing organic feedstock, comprises system of supply of initial feedstock, anaerobic bioreactor, biomass heater, biogas withdrawal system, biomass removing system, and technological process control system, where supply system of initial feedstock mechanism for disintegrating and mixing initial feedstock with initial feedstock heating system is included, consisting of receiving funnel, crushing mechanism, mixing mechanism, heating system, that ensures possibility of obtaining uniform initial mass due to use of rotor blades of installed, on two hollow shafts, which form two batteries, which have different directions of rotation.
NOVELTY - Treating biomass material involves: subjecting the biomass material to a pretreatment step to produce a pretreated biomass; cooling and adjusting the pH of the pretreated biomass; subjecting the cooled and pH controlled pretreated biomass to a first enzymatic hydrolysis step to produce a liquefaction material; contacting at least a portion of the liquefaction material with the pretreated biomass; and transferring a second portion of the liquefaction material to undergo further enzymatic hydrolysis.    USE - The method is useful for treating biomass material (claimed).    ADVANTAGE - The method is environment friendly, and efficiently controls the temperature and volume of the pretreated biomass material to the reactor while reducing the need for the addition of fresh, cooling liquid (e.g., water) to the hot pretreated biomass from the appropriate pretreatment process.    DETAILED DESCRIPTION - Treating biomass material involves: subjecting the biomass material to a pretreatment step to produce a pretreated biomass; cooling and adjusting the pH of the pretreated biomass by adding cooling liquid and pH controlling material to obtain a cooled and pH controlled pretreated biomass having a temperature and pH sufficient to allow enzymatic hydrolysis of the cooled and pH adjusted pretreated biomass; subjecting the cooled and pH controlled pretreated biomass to a first enzymatic hydrolysis step to produce a liquefaction material in an at least first vessel; contacting at least a portion of the liquefaction material with the pretreated biomass obtained from the pretreatment step as at least a portion of the cooling liquid to cool the pretreated biomass, where the liquefaction material is cooled prior to being used as at least a portion of the cooling liquid; and transferring a second portion of the liquefaction material to undergo further enzymatic hydrolysis.
NOVELTY - Separating sunflower extraction meal particles into at least one fraction with a high protein content and into at least one fraction with a high cellulose content, comprises dry separating the sunflower extraction meal using a filter and passing the particles which do not pass through the filter to the subsequent removal step. The particles pass through the filter are allocated to the fraction with a high protein content.    USE - The method is useful for separating sunflower extraction meal particles.    ADVANTAGE - The method is simple and ensures energy efficient separation of particles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plant (20) for separating sunflower extraction meal particles, comprising a device with a removal unit, and a dry separator unit, where the device does not comprise apparatus for sprinkling the particles and water.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a first part of a plant.    Plan sifters (1)    Impact mill (11)    Fluted roller mill (12)    Corrugating roller chair (13)    Plant (20)
NOVELTY - A hydrogen-producing catalyst consists of chrome compound layer, nickel chrome alloy, and microparticles containing oxygen and nickel as main component. The chrome compound layer is formed on the nickel chrome alloy, and the microparticles are distributed in the chrome compound layer.    USE - Hydrogen-producing catalyst is used for production of hydrogen (claimed) used as fuel source of domestic fuel cells.    ADVANTAGE - The hydrogen-producing catalyst has excellent catalytic performance, stability, ductility and malleability, and enables the economical production of hydrogen. The precipitation of carbon on the surface of catalyst during the manufacturing process is suppressed. The requirement of process such as pre-processing of the nickel aluminum alloy catalyst is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-producing catalyst, which involves heat-processing the nickel chrome alloy at an activation process temperature in atmosphere containing mixed gas of oxidizing gas and reducible gas; and    (2) production of hydrogen, which involves producing hydrogen using gas containing water vapor and carbon atoms in presence of the hydrogen-producing catalyst. The steam-carbon ratio during the production of hydrogen is 1-3, which is the ratio of number of water vapor molecules with respect to the number of carbon atoms contained in the gas.
NOVELTY - A method of preparing an organic fertilizer from organic substances comprises the following steps: adding the microbial odor inhibition agent into drinking water for poultry and livestock and providing the drinking to poultry and livestock, wherein the microbial odor inhibition agent can facilitate pre-fermentation of organic substances in the poultry and livestock and inhibit the odor of the organic substances, so as to form a primarily fermented organic substance; placing the primarily fermented organic substance and a fermentation additive into a mixer for mixing, so as to form a formulation raw material; filling the formulation raw material into a sealed fermentation tank to carry out anaerobic fermentation, forming a water-containing organic fertilizer after 7 to 15 days; performing solid/liquid separation on the water-containing organic fertilizer to produce an organic fertilizer semi-finished product and an aqueous fertilizer, wherein the aqueous fertilizer is useful as a water fertilizer for plants; and dispensing the organic fertilizer semi-finished product after drying, so as to produce an organic fertilizer finished product. Therefore, the air pollution caused by organic substances can be eliminated during the process, and the organic substances can be rapidly converted into odorless and non-toxic organic fertilizer.
NOVELTY - Composite plant for producing chemical product, comprises a combined air separation- and carbon dioxide separating plant (1) for obtaining at least carbon dioxide and nitrogen, and an electrolysis unit (2) for producing hydrogen. The carbon dioxide obtained in the combined air separation- and carbon dioxide separating plant is used for producing chemical products.    USE - The composite plant is useful as a chemical storage for fluctuating renewable energies and for producing chemical products (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a control unit, which controls the composite system;    (2) producing chemical products comprising obtaining intermediates for producing chemical products at least partially in the combined air separation- and carbon dioxide separating plant and the electrolysis unit of the composite plant, and converting into the chemical products; and    (3) a computer program product for controlling the composite system.    DESCRIPTION OF DRAWING(S) - The figure 2 shows a schematic representation of the composite plant.    Air separation- and carbon dioxide separating plant (1)    Electrolysis unit (2)    Unit (3)    Energy (E)
NOVELTY - Special organic bio-fertilizer comprises raw materials comprising 3-7 pts. wt. herba equiseti hiemalis, 1-7 pts. wt. nettle leaves, 1-7 pts. wt. licorice, 10-20 pts. wt. chicken manure, 5-20 pts. wt. carbon soil, 1-7 pts. wt. wheat bran and 0.5 wt.% fermented strain.    USE - The special organic bio-fertilizer is useful for rice seedling (claimed).    ADVANTAGE - The bio-fertilizer can be prepared simply and cost-effective, promotes rice seed germination and seedling growth, improves quality of rice seedling, and controls seedling disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bio-fertilizer, which involves mixing the raw materials, maintaining water content to 40-55%, adding the mixture into closed plastic barrel, fermenting the mixture at high temperature, turning mixture for 3-5 times, and fermenting for 50 days.
NOVELTY - Preparing venlafaxine intermediate compound (I) comprises (i) performing reduction reaction of (1-hydroxy-cyclohexyl)-(4-methoxy-phenyl)-acetonitrile (II), borohydride and aluminum trichloride in diethylene glycol dimethyl ether medium; and (ii) adding toluene, then adding the mixed solution into water, performing hydrolysis, adjusting pH to 9-12 using sodium hydroxide, allowing for stratification and concentrating the organic layer to obtain (I), where the molar ratio of (II), borohydride and aluminum trichloride is 1:1.8-4:1-1.4.    USE - The method is useful for preparing venlafaxine intermediate compound (claimed).    ADVANTAGE - The method improves the conversion rate of raw materials, reduces the use amount of the solvent, which greatly reduces the environmental pollution, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing venlafaxine intermediate compound of formula (I) comprises (i) performing reduction reaction of (1-hydroxy-cyclohexyl)-(4-methoxy-phenyl)-acetonitrile of formula (II), borohydride and aluminum trichloride in diethylene glycol dimethyl ether medium at 40-80 degrees C; and (ii) adding toluene, then adding the mixed solution into water, performing hydrolysis, adjusting pH to 9-12 using sodium hydroxide, allowing for stratification and concentrating the organic layer to obtain (I), where the molar ratio of (II), borohydride and aluminum trichloride is 1:1.8-4:1-1.4, the volume of diethylene glycol dimethyl ether is 2-5 ml/g of (II), the volume of toluene is 6-10 ml/g of (II), and the volume of water is 5-8 ml/g of (II).
NOVELTY - The utility model claims a tail gas purifying function one's environment-friendly fermenting tower, comprising a tower body, a fermenting bed, fermenting bed is provided with at least more than two layers, from up to down is installed on the tower body, the tower body is provided with a feeding port and a discharging port, upper tower body is further equipped with upper working space with the tower body inner space's tail gas purifying device, the tail gas purifying device is capable of taking fermented tail gas purifying processing, environment-friendly emission's, tail gas purifying device's inlet end or outlet end is connected with the fan. The utility model's fermenting tower can realize fermented tail gas purifying, meets environmental requirement to improve the fermentation efficiency.
NOVELTY - Polypeptide having beta -glucosidase activity of amino acid sequence of SEQ ID NO: 1 (a 744 amino acid sequence fully defined in the specification), is new.    USE - The polypeptide is useful in an isolated host cell for the hydrolysis of beta -oligosaccharides and of cellobiose to glucose and for the production of biofuel (all claimed).    ADVANTAGE - The polypeptide has less sensitive to inhibition by glucose, and retains improved beta-glucosidase activity in the presence of high concentration of glucose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) purified or isolated nucleic acid encoding the polypeptide;    (2) a vector comprising the nucleic acid;    (3) an isolated host cell comprising the polypeptide, the nucleic acid, or the vector;    (4) an enzyme composition acting on the lignocellulosic biomass, where the enzyme composition is produced by filamentous fungi and comprises the polypeptide; and    (5) producing biofuel from biomass, comprising suspending the material in an aqueous phase, then hydrolyzing in the presence of the enzymatic composition or the cell of the biomass lignocellulose to produce a hydrolyzate containing glucose, fermenting the hydrolyzate of the glucose to produce a fermentation broth, separating biofuel from the fermentation broth, where the hydrolysis and fermentation steps are carried out simultaneously.
NOVELTY - The mixer has transmission shaft (2) that is connected with the gear box. The gear box is connected with the box by the stirring teeth (17) of the upper gear box. A gear box is connected with another gear box to rotate along rotating direction of the stirring teeth agitating machine. The transmission bevel gear drives the left and right stirring gear to rotate along the rotating direction of the stirring teeth of the stirring mill.    USE - Mixer used in livestock and poultry breeding industry.    ADVANTAGE - The mixing and stirring effect of the mixer can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the mixer.    Transmission shaft (2)    Tank (3)    Oil pump (4)    Transmission gear (10)    Stirring teeth (17)
NOVELTY - Kiln or blast furnace gas phosphoric acid method to produce synthetic ammonia comprises water bath cooling kiln or blast furnace phosphoric acid gas, removing phosphorus steam and most dust through venturi tube and fog removing device, subjecting to wet oxidation desulfurization, converting the nitric oxide, carbon monoxide, and water in the tail gas in the presence of catalyst into hydrogen and nitrogen at 2.5-2.9:1 mol ratio, obtaining synthetic ammonia raw material gas, subjecting to desulfuration, decarburization, and gas purification, and producing synthetic ammonia.    USE - Kiln or blast furnace gas phosphoric acid method to produce synthetic ammonia (claimed).    ADVANTAGE - The method achieves comprehensive raw material utilization, eliminates environmental pollution, and is simple.
NOVELTY - A Koji saccharified enzyme is fermented by performing living cell suspension to koji saccharified enzyme, immobilizing living cell embedding, embedding in bran and old rice bran, making immobilized enzyme, fermenting into ball shape, putting into organic garbage, excrements, and other organic substrates, and performing fermentation action with koji saccharified enzyme to turn into feed or organic fertilizer.    USE - Fermentation of koji saccharified enzyme for turning organic garbage and excrements into animal feed and organic fertilizer (claimed).    ADVANTAGE - Process reduces pollution in environment by making garbage and excrements into useful products.    DESCRIPTION OF DRAWING(S) - The drawing shows a method of flow diagram of Fermentation of koji saccharified enzyme. (Drawing includes non-English language text).
NOVELTY - Special fertilizer comprises raw materials comprising 20-30 pts. wt. straw, 1-5 pts. wt. sugar, 1-5 pts. wt. microbial inoculum, 5-25 pts. wt. ammonium sulfate, 5-20 pts. wt. potassium dihydrogen phosphate, 5-20 pts. wt. diammonium hydrogen phosphate and 5-20 pts. wt. potassium sulfate.    USE - The special fertilizer is useful for peanut (claimed).    ADVANTAGE - The fertilizer has nitrogen fixation, promotes growth of B.megaterium and improves whole bacteria fixation ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves inoculating microbial inoculum of nitrogen fixation Bacillus megaterium and nitrogen fixation Bacillus into liquid culture medium to obtain microbial inoculum, and inoculating to straw stack.
NOVELTY - Rapeseed cake fermented agricultural organic fertilizer involves adding medicine wine, nitrogen fertilizer, calcium superphosphate and water, preparing mother liquor (I), stirring uniformly, adding rape seed cake to mother liquor, soaking for 15-30 days, adding water, and fermenting for 3-20 days.    USE - Rapeseed cake fermented agricultural organic fertilizer is used for agricultural crops, vegetable crops, cash crops or fruit crops (all claimed).    ADVANTAGE - The rapeseed cake fermented agricultural organic fertilizer has high fat content of organic material, and is convenient for transporting, and can be manufactured efficiently and economically in short period of time. The rapeseed cake fermented agricultural organic fertilizer effectively improves quality and yield of agricultural products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of rapeseed cake fermented agricultural organic fertilizer. Medicine wine, nitrogen fertilizer and calcium superphosphate are mixed uniformly, and water is added to mother liquor (I), and stirred uniformly, such that the weight ratio of medicine wine, nitrogen fertilizer, calcium superphosphate and water is 0.01-0.05:0.5-3:20-70:100-400. The content of pure nitrogen in nitrogen fertilizer is 10-47%. The obtained mother solution is added with rape seed cake, soaked for 15-30 days, and water is added and stirred at 20-30 degrees C to ferment for 7-10 days to obtain rapeseed cake fermented agricultural organic fertilizer; and    (2) application of rapeseed cake fermented agricultural organic fertilizer, which involves uniformly mixing cake for agricultural organic fertilizer and chemical fertilizer urea, obtaining composite fertilizer, fertilizing according to different growth period of fruit, and harvesting after 3-4 months.
NOVELTY - A composite bio-fertilizer comprises 1 pt. wt. Bacillus, 1-10 pts. wt., preferably 4-6 pts. wt. lactic acid bacteria, 1-10 pts. wt., preferably 4-6 pts. wt. Saccharomycetes, 10-30 pts. wt., preferably 15-25 pts. wt. organic fertilizer, 10-30 pts. wt., preferably 15-25 pts. wt. inorganic fertilizer, and 1-10 pts. wt., preferably 2-8 pts. wt. binder.    USE - Composite bio-fertilizer is used in farming and animal husbandry, and aquaculture.    ADVANTAGE - The composite bio-fertilizer exhibits stable performance characteristics and wide functionality, is nontoxic and environmentally-friendly, and does not cause any side effects. The total effective viable count is 4000 million/g or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite bio-fertilizer, which involves preparing bacteria solution using Bacillus, lactic acid bacteria, and Saccharomycetes, mixing organic fertilizer and inorganic fertilizer, adding the bacteria solution, mixing uniformly, adding binder, mixing uniformly, drying, and granulating.
NOVELTY - A 2-(4,6-dimethylpyrimidin-2-ylcarbamoylsulfamoyl)benzoic acid methyl ester is prepared by mixing o-benzoyl sulfimide, dimethyl carbonate and catalyst A at 70-120 degrees C under anaerobic condition resulting to N-sulfonylimine derivative, adding methanol and catalyst B at 20-120 degrees C, and adding o-carbomethoxybenzene sulfonamide and 4,6-dimethylpyrimidine in organic solvent at 100-105 degrees C.    USE - Method for preparing 2-(4,6-dimethylpyrimidin-2-ylcarbamoylsulfamoyl)benzoic acid methyl ester (claimed).    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production. It results to product with not less than 95% purity and not less than 55% yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM further includes preparation of 2-(4,6-dimethylpyrimidin-2-ylcarbamoylsulfamoyl)benzoic acid methyl ester comprising distilling, cooling to 40 degrees C, neutralizing, filtering, and drying.
NOVELTY - Method for producing sulfur effective microorganisms (EM) fermented fertilizer involves (a) preparing fructose solution, adding EM to the solution and culturing under aerobic conditions to obtain EM solution, (b) adding solution obtained in (a), phosphoric acid and potassium to fertilizer to obtain EM fertilizer solution, (c) fermenting, (d) boiling sulfur, salt and sodium hydroxide, to obtain sulfur solution and (e) adding fermented EM fertilizer solution to sulfur solution.    USE - The method is useful for producing sulfur EM fermented fertilizer for crops chosen from rice, potatoes, apple, edible roots, garlic, sesame, Platycodon grandiflorous, and sweet potato (all claimed).    ADVANTAGE - The sulfur EM fermented fertilizer improves taste and increases nutrient content, quality and yield of agricultural products and helps in long-term storage of the products.    DETAILED DESCRIPTION - Method for producing sulfur effective microorganisms (EM) fermented fertilizer involves (a) adding 100 pts. wt. water to 0.1-2 pts. wt. fructose to obtain fructose solution, adding 5-20 pts. wt. EM to the solution and culturing at 29-35 degrees C for 1-5 days under aerobic conditions to obtain EM solution, (b) adding 100 pts. wt. solution obtained in (a), 30-50 wt.% phosphoric acid and 50-70 wt.% potassium to 150-250 pts. wt. fertilizer to obtain EM fertilizer solution, (c) fermenting at 25-33 degrees C for 10-30 days and cooling to 7-12 degrees C, (d) adding 100 pts. wt. water to 40-60 pts. wt. sulfur, 0.5-2 pts. wt. salt and 30-50 pts. wt. sodium hydroxide, and boiling to obtain sulfur solution and (e) adding 100 pts. wt. fermented EM fertilizer solution to 0.1-5 pts. wt. sulfur solution and 0.01-0.5 pts. wt. sulfur and maintaining at low temperature to obtain sulfur EM fermentation fertilizer.
NOVELTY - Manufacture of 4-acetoxy-2-methyl-2-butenal involves performing Morita-Baylis-Hillman reaction of ethylene oxide and acrolein in organic solvent under the action of phosphine reagent, obtaining allyl alcohol compound (I), reacting obtaining product with acetylating agent, performing acylation reaction, obtaining aldehyde ester (II) and performing transposition reaction of obtained product in presence of double-bond transferring catalyst and hydrogen.    USE - Manufacture of 4-acetoxy-2-methyl-2-butenal (claimed).    ADVANTAGE - The method efficiently provides 4-acetoxy-2-methyl-2-butenal by simple and economical process with suppressed generation of three waste.    DETAILED DESCRIPTION - Manufacture of 4-acetoxy-2-methyl-2-butenal involves performing Morita-Baylis-Hillman reaction of ethylene oxide and acrolein in organic solvent under the action of phosphine reagent, obtaining allyl alcohol compound of formula (I), reacting obtaining product with acetylating agent, performing acylation reaction, obtaining aldehyde ester of formula (II) and performing transposition reaction of obtained product in presence of double-bond transferring catalyst and hydrogen. The phosphine reagent is of formula: PR1R2R3.    R1-R3=1-5C alkyl or phenyl.
NOVELTY - Temperature reduction of methanation catalyst using hydrogen gas comprises reacting carbon-containing gas and hydrogen, heating at 450 degrees C and raising temperature to 500-600 degrees C for less than 2 hours.    USE - Method of reducing temperature of methanation catalyst (claimed).
NOVELTY - Performing culturing process using culture material made of organic sludge, involves inoculating indigenous microbes to bread crumbs, fermenting, mixing fermented product with extracts of e.g. common reed, fermenting again to obtain first culture, mixing soil and organic sludge, further mixing fermented product to mixture, incubating to obtain second culture, mixing first and second cultures, and performing fermentation of mixture to obtain final culture.    USE - The method is useful for performing culturing process using culture material made of organic sludge (claimed).    ADVANTAGE - The method is completely utilizes organic sludge.    DETAILED DESCRIPTION - Method for performing culturing process using culture material made of organic sludge, involves inoculating indigenous microbes to bread crumbs, fermenting for 5-7 days, mixing fermented product with extracts of purple eulalia, common reed, dandelion, parsley leaf, plantain, bellflower, pine needle, pine pollen, rosin, Salicornia, mugwort, Codonopsis, amaranth and humus extract, fermenting again at 20-25 degrees C for 5-7 days to obtain first culture, mixing soil and organic sludge containing soybean paste, meju, soybean, soy sauce, kimchi, rice wine and fermented milk, further mixing the fermented product to the mixture, incubating at 55-60 degrees C for 18-21 days to obtain second culture, mixing first and second cultures, and performing fermentation of mixture at 55-60 degrees C for 5-7 days to obtain final culture. An INDEPENDENT CLAIM is included for compost which comprises culture material comprising organic sludge.
NOVELTY - The pelletizing device has a frame portion (100) for supporting a pellet generating unit (200) arranged along the gravity direction. The pellet generating unit generates pellet compost by extruding fertilizer raw material along gravity direction, according to the power received from a power supply unit (300). The pellet generating unit includes a hopper (220) coupled to the upper end of a cylinder (230), for collecting and supplying fertilizer raw material to the cylinder. The pellet generating unit has a screw supporting unit (249) that supports the screw installed at housing (210).    USE - Compost pelletizing device.    ADVANTAGE - The compost pelletizing device efficiently collects the extruding water and processes the water without lowering its quality. The pelletizing device can be fitted according to the raw material state and can be driven efficiently. The operation and maintenance of apparatus can be carried out conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the compost pelletizing device.    Frame portion (100)    Pellet generating unit (200)    Housing (210)    Hopper (220)    Cylinder (230)    Screw supporting unit (249)    Power supply unit (300)
NOVELTY - This utility model claims a kind of energy-saving high sewage treatment device, comprising a sewage tank and a heating water tank of solar heater, the solar heater comprises a solar energy vacuum heat collecting pipe, a heat storage water tank, a connecting pipeline and a heat exchanger in the sewage pool, the solar vacuum heat collecting pipe is used for the hot water in the tank heating, heat storage water water tank is connected with the heat exchanger by a connecting pipeline. This utility model use solar energy, wind energy complementary energy storage device for sewage, improves the activity of the microorganism, enhances the processing efficiency of the sewage. A sewage by a temperature control device the best active temperature, the micro-organism treatment efficiency of sewage reach the best meets the sewage treatment plant for processing the sewage, at the same time, the equipment is simple, maintenance is convenient, environment-friendly and efficiency is high.
NOVELTY - The device has integrated monitoring display meter (10) that is provided on sealing cover injection hole provided on elliptic seal head dome shaped structure of marsh gas fermentation tank (18). A residual input pipe is sleeved on center portion to bottom of the tank. The residual input pipe is connected with the biogas pump (17) set on the top center of tank. A stirring mixing tank (2) is connected with the raw material storage tank (1) and set in parallel on one side of fermentation tank. The desulfurizing tanks are set in parallel with regard to fermentation tank.    USE - Marsh gas fermentation device installed on underground concrete pouring sandwich composite structure of cylindrical fermentation tank, used in large biogas fermenting system for producing pure straw.    ADVANTAGE - The structure of the marsh gas fermentation device can be simplified.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas ferment device.    Raw material storage tank (1)    Stirring mixing tank (2)    Monitoring display meter (10)    Biogas pump (17)    Fermentation tank (18)
NOVELTY - System comprises an opening at one end of tank body (1). The inner wall of the tank body is provided with a heating pipe (9). The opening end of the tank body is provided with a top film (5) to form a storage region. The tank body of the marsh gas producing system is provide with a stirring device (7). The stirring device is provided with a motor set on the external part of the motor. The upper part of the tank body is provided with a feeding port (2) and a liquid outlet port (8). The liquid outlet port is set on the feeding port.    USE - System for producing methane.    ADVANTAGE - The system enables to improve the production of marsh gas, and is cost effective.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a marsh gas producing system.    Tank body (1)    Feeding port (2)    Top film (5)    Stirring device (7)    Liquid outlet port (8)    Heating pipe (9)
NOVELTY - A kind of clean marsh gas ferment device, comprises a storage chamber, a feeding pool, a fermenting tank, a discharge tank, a sedimentation tank, a separation tank, a purifying pond. Storage pool collect decomposed livestock excrement, straw and so on, so as to fully decay deposition, starting the delivery pump in set time to decay deposit to control a feeding pool, to make it reach the best ferment state, every day. pump the first time for the material in the fermentation tank to carry out biological fermentation to produce biogas, and automatically discharge a deposition to the discharging tank, and when it reaches a certain amount of automatic discharged to the sedimentation tank continuing using the PEG precipitation, liquid into purifying pond, the solid to a bio-fertilizer production device processed into granules by delivery pump. The purifying pond for purifying the biogas slurry to make it reach the standard of drinking water for agricultural irrigation.
NOVELTY - Method for producing straw and biodegradable garbage biogas, involves (a) mixing straw and biodegradable garbage to form acid, (b) raising temperature of the acid under anaerobic environment to produce methane, and (c) carrying out circulation and comprehensive utilization to obtain biogas.    USE - The method is useful for producing straw and biodegradable garbage biogas (claimed).
NOVELTY - Processing tobacco waste, involves mixing tobacco waste and water, adding activated sludge, Acinetobacter (CGMCC 7.47), and signaling molecules to mixture, and performing aeration in the mixture for 18-48 hours, where composition of signaling molecules comprises 8-16 mmol/l N-3-oxo-L,-hexanoyl-homoserine lactone, 4-8 mmol/l N-hexanoyl-homoserine lactone in volume ratio of 2:1-1:2.    USE - The method is useful for processing tobacco waste (claimed).    ADVANTAGE - The method is environmentally-friendly, and fast and efficient in degrading nicotine or 4-aniline in the organic fluorine-containing waste water in the tobacco waste, has excellent durability, and reduces harm.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating organic wastewater fluorine, which involves mixing waste water to the activated sludge, Acinetobacter, signaling molecules, and aerating the mixture for 24-72 hours.
NOVELTY - The method involves starting sequencing batch reactor (SBR) denitrification reactor, when the water reaches the set ratio. A pH sensor value is received by programmable process controller and is transmitted to computer. A feeding pump is started. The feeding pump is closed, when the pH value is positive. The water inlet valve and water outlet valve are started by adjusting the working time of SBR denitrification reactor. A mud discharging valve is closed, when concentration of nitrite nitrogen and nitrate nitrogen is more than 80%.    USE - Method for realizing domestic sewage short-range nitration through sludge attenuation.    ADVANTAGE - The short-range nitration effect is stabilized, and the operation cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of realizing domestic sewage short-range nitration. (Drawing includes non-English language text)
NOVELTY - Processing sewage involves processing waste water by separating solid-liquid by separator. The liquid is transferred in purification tank at pH 7-8, and then microbial preparation 20/cubic meter is added in tank daily for a week and then for five days for filtration to obtain the desired solution. The microbial agent comprises active component and carrier, where active component comprises (in pts.wt.): nitrosobacteria (10), sulfur nitride (8), Pseudomonas stutzeri (7), Acidithiobacillus ferrooxidans (6) and Bacillus licheniformis (5).    USE - Method for processing sewage obtained during livestock cultivation (claimed).    ADVANTAGE - The sewage processing method is economical and has removal rate of ammonia, nitrogen and phosphorus is greater than or equal to 99%.    DETAILED DESCRIPTION - Processing sewage involves processing waste water by separating solid-liquid by separator. The liquid is transferred in purification tank at pH 7-8, and then microbial preparation 20/cubic meter is added in tank daily for a week and then for five days for filtration to obtain the desired solution. The microbial agent comprises active component and carrier, where active component comprises (in pts.wt.): nitrosobacteria (10), sulfur nitride (8), Pseudomonas stutzeri (7), Acidithiobacillus ferrooxidans (6), Bacillus licheniformis (5), Phanerochaete chrysosporium (3), Arthrobacter (2) and Rhodococcus sp. (2), and carrier comprises turfy soil, sawdust and diatomite in mass ratio of 3:2:1. Microbial agent is prepared by mixing and stirring active component and carrier in weight ratio of 1:1. The obtained material is heated at 4 degrees C and dried to obtain 8-10% water content.
NOVELTY - The device has horizontal working table (1) that is placed on constant temperature magnetic stirrer (2) used for collecting marsh gas. A collecting container (7) is provided with a collecting port. The upper cavity of the collecting container is provided with a laser range finder (13). The constant temperature magnetic stirrer is connected with a rotating speed sensor (14). Collecting pipes (16,17) are respectively provided with two electromagnetic valves (18,19) that are connected with programmable logic controller (PLC) provided in horizontal working table.    USE - Experimental device for generating marsh gas under different stirring speed detection.    ADVANTAGE - The experiment device can be provided with high accuracy experiment, and the high automation level can be obtained. The high experiment precision can be achieved, and the convenient operation can be obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for experimental method for generating marsh gas used for boiling water and cooking based on different stirring speed detection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the experimental device for generating marsh gas under different stirring speed detection.    Horizontal working table (1)    Constant temperature magnetic stirrer (2)    Collecting container (7)    Laser range finder (13)    Rotation speed sensor (14)    Speed sensor (15)    Collecting pipes (16,17)    Electromagnetic valves (18,19)
NOVELTY - Method of fermentation involves taking the cassava and corn mixed powder, adding water, adding wastewater in anaerobic water outlet, water and distilled water, to obtain mixed slurry; adding high temperature amylase to the mixed slurry, stirring them uniformly, heating, to obtain liquefied slurry; reducing the temperature to 32-34 degrees C, then adding maltogenic amylase and active dry yeast, mixing, carrying out fermentation, to produce alcohol; separating the alcohol by solid-liquid separation to separate slag, entering the remaining liquor into marsh gas.    USE - For producing alcohol and marsh gas (claimed).    ADVANTAGE - The process has improved production efficiency, and reduced production cost; reduces sewage discharge in the alcohol production; not only saves water and sewage treatment cost, but also generates more additional product, which brings aconsiderable market economic benefit; and is environment-friendly.    DETAILED DESCRIPTION - Method of fermentation involves taking the cassava and corn mixed powder, adding water, adding wastewater in anaerobic water outlet, water and distilled water, to obtain mixed slurry; adding high temperature amylase to the mixed slurry, stirring them uniformly, heating at 95 degrees C for 100 minutes, to obtain liquefied slurry; reducing the temperature to 32-34 degrees C, then adding maltogenic amylase and active dry yeast, mixing uniformly, controlling the temperature to 33-34 degrees C, carrying out fermentation, then distilling to produce alcohol; separating the alcohol by solid-liquid separation to separate slag, entering the remaining liquor into marsh gas, fermenting, and recycling, to obtain biogas.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of method of fermentation. Drawing includes non-English language text.
NOVELTY - Pure oxygen biological fluidized reaction sewage processor, comprising a main body tank, a lifting pump, a connecting pipe, and a main body tank is cylindrical, the inner cavity of the middle upper part is equipped with a guide cylinder along the perpendicular bisector, the guide tube is sleeved outside the flow tube between them to form an interlayer cavity, guide cylinder is fixedly connected the lower opening of the guide plate, the lower end and the horizontal baffle plate edge of the guide plate is fixedly connected with the inner wall of the main tank body, a horizontal baffle plate is fixedly connected with one of the upper part is less than the horizontal clapboard of the cone mixing chamber, a middle position of the inner wall of the cavity of the cone is welded with the upper part small and the lower opening of the gas-water mixing outlet, the periphery of the shunting cylinder is filled with particle active carbon, a horizontal baffle plate is set with a plurality of filter head, lift pump in the main body tank, and the outlet of a cone cavity through the water cut, provided with a stop valve, a jet device is installed on the two ends of the stop valve, the inlet is connected with the lifting pump water tube cut to one side of the outlet of the cone cavity, a device for a pure oxygen inlet.
NOVELTY - This utility model claims a kind of crop by-product energy and using system, comprising a raw material machine, a feeding device, a marsh gas generating device, a sewage purifying and separating device, and solar energy and marsh gas heating device, wherein the sewage purifying separating device comprises a sedimentation tank, sedimentation tank is connected with the dehydration purifying pond, the water pump is set with the dewatering purifying pond, the water pump is connected with a sewage purification and separation tower, and separating tower is connected with the raw material tank for purifying sewage. The environment pollution, resource utility model for the farmer to the vegetable highland barley seed of crop by-product, vegetable leaf, melon stem, crop crops highland barley, straw and so on as improper processing caused by the waste and inconvenience of various energy sources to provide a full use of the straw in the presence of, but also can prevent burn, rot and so on caused by the environment pollution of crops by-product energy recycling system.
NOVELTY - This utility model claims a kind of self-adapting type marsh gas generating collecting system, comprising a marsh gas tank and a marsh gas collector, a methane tank comprises main tank, a feed port and a discharge port, a marsh gas collector is located in the main tank, a marsh gas collector is provided with a downward opening of the cavity and located between the side wall of the air outlet nozzle, a marsh gas collector and the top of the main tank there is a gap, is submerged to form a marsh gas chamber for collecting and storing biogas in a biogas slurry, the utility model self-adapting type marsh gas generating collecting system in the marsh gas chamber pressure is strong, but the residual air and marsh gas in large molecular weight of the impurity gas extruding a marsh gas room, a marsh gas collector and the side wall gap is easily discharged to obtain methane with high purity high marsh gas, and the high pressure gas high efficiency to a tank. In addition, there is a gap because of marsh gas collector and the side wall, move back and forth action of the biogas slurry and stirring the gas which can effectively prevent the crust of the main pool surface scum from marsh gas chamber.
NOVELTY - This utility model claims a kind of livestock and poultry waste dry fermentation anaerobic reactor, aiming at providing a kind of compact and reasonable structure, saves the water resource and energy-saving, high fermentation efficiency of livestock and poultry waste dry fermentation anaerobic reactor. A fermentation tank, a liquid storage tank, the fermentation tank is designed to be circular column shape cavity structure, wherein the fermentation tank are sleeved is provided with liquid storage tank, the one side of the bottom of the fermentation tank is provided with a feeding hopper and a feeding spiral conveyer, the other one side of the bottom of the fermentation tank is provided with a discharging spiral conveyor, a discharging spiral conveyer is corresponding to the top of the fermentation tank is provided with solid-liquid separating device is provided with extends into the bottom of the liquid storage tank through the return pipe in solid-liquid separation device, the fermentation tank is provided with a spraying humidifying device and mixing device. This utility model is suitable for livestock and poultry waste is dry anaerobic fermentation to generate marsh gas.
NOVELTY - Preparing earthworm feeding substrate comprises adding material and pig manure with water, uniformly stirring and mixing the material, adding stirred material with thermophilic side spore, Trichoderma reesei and Trichoderma viride and sucrose, uniformly stirring the material and then mixing with acetic acid solution to adjust pH value, carrying out garbage fermentation using oxygen supplying system and fermentation process, drying the mixture with moisture, crushing the material into fine powder, and adding straw ferment rotten powder and sand soil.    USE - The method is useful for preparing earthworm feeding substrate (claimed).    ADVANTAGE - The method effectively and rapidly prepares the earthworm feeding substrate in an eco-friendly manner with improved yield and quality.    DETAILED DESCRIPTION - Preparing earthworm feeding substrate comprises adding 30-40 wt.% of material and 8-12 wt.% of pig manure with balance amount of water, uniformly stirring and mixing the material, adding stirred material with 3-8 wt.% of thermophilic side spore, Trichoderma reesei and Trichoderma viride having viable count of more than 1x 109/g and 0.5-2 wt.% of sucrose, uniformly stirring the material and then mixing with 4-6 wt.% of acetic acid solution to adjust pH value of 5-6, carrying out garbage fermentation using oxygen supplying system at 25-28 degrees C for 48 hours and fermentation process at 50-60 degrees C for 49-168 hours, drying the mixture with moisture content of lower than 12%, crushing the material into fine powder of 60-80 meshes sieve, adding straw ferment rotten powder and sand soil with ratio of 1-2:1-2.
NOVELTY - A fluid catalytic cracking (FCC) catalyst is produced by adding nitrifying bacteria in microorganism carrier with less than or equal to 5000 mg/L activated sludge of sewage treatment plant, and adding denitrifying agent when system of nitrate-nitrogen total nitrified product is greater than or equal to 50% in which FCC catalyst concentration is 200-1000 mg/L, chemical oxygen demand (COD) concentration is less than or equal to 500 mg/L, sewage treatment temperature is 18-40 degrees C, dissolved oxygen 0.1-4 mg/L, and pH is 7-9.    USE - Production of fluid catalytic cracking catalyst (claimed).    ADVANTAGE - Production process has high efficiency, discharged ammonia and other pollutants, and stable denitrification treatment.
NOVELTY - A wastewater is denitrified by adding nitrifying bacteria in microbial carrier with less than or equal to 5000 mg/L concentration of activated sludge from sewage treatment plant, adding denitrifying agent when system contains greater than or equal to 50% nitrate nitrogen of total nitrified product, ending of start-up stage when ammonia nitrogen and nitrate nitrogen concentration is less than or equal to 50 mg/L, and stable operating. Denitrifying agent contains Arthrobacter creatinolyticus FDN-1 (CGMCC 3657), Flavobacterium mizutaii FDN-2 (CGMCC 3659), and Paracoccus denitrificans DN-3 (CGMCC 3658).    USE - Denitrification of wastewater (claimed).    ADVANTAGE - Denitrification process has high efficiency, improved wastewater nitrogen removal, and achieved outstanding treatment effect.
NOVELTY - Microbial degradation of catering industry sewage pipeline comprises culturing Pseudomonas, oats food acid bacteria, Alcaligenes, and Bacillus in bacterial growth culture medium to form aggregates of microorganisms; and subjecting to microbial polymer acclimatization with 20 g/L animal fats and vegetable oils containing bacterial growth culture medium, expanding, and adding 1 wt.% to sewage draining pipeline.    USE - Method for microbial degradation of catering industry sewage pipeline (claimed).    ADVANTAGE - The method has long survival time of biological activity of microbial inoculum and high resistance to impact loads water quality.
NOVELTY - Treating wastewater comprises degrading organic matter under a presence of ammonia-nitrogen using microbial inoculum including Kocuriapalustris (FSDN-A), Arthrobacter creatinolyticus (FDN-1), Flavobacterium mizutaii (FDN-2), Paracoccusdeni trificans (DN-3) and Methylobacterium phylosphaerae (SDN-3) with preservation number of CGMCC N0.5061, CGMCC N0.3657, CGMCC N0.3659, CGMCC N0.3658 and CGMCC No. N0.3660, respectively.    USE - The method is useful for treating wastewater (claimed).    ADVANTAGE - The method treats wastewater with simple operation without secondary pollution in a safe and eco-friendly manner.
NOVELTY - A high-salt-content wastewater catalytic agent is biodenitrified by adding nitrifying bacteria in microbial carrier with less than or equal to 4000 mg/L concentration of activated sludge from sewage treatment plant in which starting temperature during operation is 18-40 degrees C, dissolved oxygen is 0.1-4 mg/L, and pH is 7-9, adding denitrifying agent when system contains greater than or equal to 50% nitrate nitrogen of total nitrified product, ending of start-up stage when ammonia nitrogen and nitrate nitrogen concentration is less than or equal to 50 mg/L, and stable operating.    USE - Biodenitrification of high-salt-content wastewater catalytic agent for wide range of wastewater quality.    ADVANTAGE - Biodenitrification process has high efficiency, improved absorbing performance, good for salinity and metal ion, reduced water turbidity, and improved wastewater treatment effect.    DETAILED DESCRIPTION - A high-salt-content wastewater catalytic agent is biodenitrified by adding nitrifying bacteria in microbial carrier with less than or equal to 4000 mg/L concentration of activated sludge from sewage treatment plant in which starting temperature during operation is 18-40 degrees C, dissolved oxygen is 0.1-4 mg/L, and pH is 7-9, adding denitrifying agent when system contains greater than or equal to 50% nitrate nitrogen of total nitrified product, ending of start-up stage when ammonia nitrogen and nitrate nitrogen concentration is less than or equal to 50 mg/L, and stable operating. Denitrifying agent contains Staphylococcus cohnii FSDN-C (CGMCC 5062), Arthrobacter creatinolyticus FDN-1 (CGMCC 3657), or Flavobacterium mizutaii FDN-2 (CGMCC 3659).
NOVELTY - Treating sewage involves setting water inlet system containing water inlet pipe via sewage enters the biological reacting system; conducting biological reaction system which is divided into anoxic zone, anaerobic zone and aerobic zone, and deposition zone, each zone in the active sludge by using microorganism to degrade the metabolic organic substance into inorganic nitrogen and phosphorus removal; carrying out sedimentation in sedimentation tank, mud-water separation and disinfection in disinfection tank, sterilizing, and killing pathogenic microorganism and collecting by outlet pipe.    USE - For treating sewage (claimed).    ADVANTAGE - The method has small civil engineering investment, compact structure, and high accuracy of pigment application; and has controllable stable process optimization, denitrification and dephosphorization effect, and high organic pollutant removing effect.    DETAILED DESCRIPTION - Treating sewage involves setting water inlet system containing water inlet pipe via sewage enters the biological reacting system pre-thick thin grid and rotational flow grit chamber; conducting biological reaction system which is divided into anoxic zone, anaerobic zone and aerobic zone, and deposition zone, each zone in the active sludge by using microorganism to degrade the metabolic organic substance into inorganic nitrogen and phosphorus removal; carrying out sedimentation in sedimentation tank, carrying out mud-water separation, clarifying the water; carrying out disinfection in disinfection tank, sterilizing, and killing pathogenic microorganism and collecting by outlet pipe.
NOVELTY - The treatment device has a horizontal mechanical stirring device that is set in a fermentation tank main body, and a temperature control system (9) that is set on the side wall of the fermentation tank body. The material is crushed by a pulverizing device and stirred by the horizontal mechanical stirring device in the fermentation tank main body. The overflow of material by a floating water forced circulation system is transported back to the fermentation tank main body through a feeding device.    USE - Solid organic waste anaerobic biological treatment device for mechanical and hydraulic combination stirring.    ADVANTAGE - Provides for high gas generating efficiency, simple operation, low cost, effective mass transfer, and high-concentration fermentation, which reduce material in the fermentation process. Realizes high speed feeding and liquid level real time monitoring and control.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the air conveying feeding device, a fermentation tank main body, and a floating hydraulic forced circulation system.    Material conveying pipe (2)    Liquid level (8)    Temperature control system (9)    Circulating pump (11)    Overflow discharge hole (33)
NOVELTY - Rapidly decomposing animal manure comprises preparing a microbial composition comprising Bacillus subtilis, Candida utilis, and lactic acid bacteria; spreading the microbial composition evenly into the animal manure fermentation bed; pouring water into the fermentation bed; and allowing the bacteria to come into contact with the manure thus decomposition occurs.    USE - The method is used for rapidly decomposing animal manure (claimed).    ADVANTAGE - The method is for decomposing animal manure is rapid and environment-friendly.
NOVELTY - Preparing nitrifying bacteria comprises (a) obtaining sludge, washing, and dehydrating; (b) dissolving polyvinyl alcohol, sodium alginate and other additives in water, heating, mixing, and cooled to 5-40 degrees C; (c) obtaining the strain; (d) adding fixative; (e) washing, and dehydrating; (f) storing at 0-10 degrees C; and (g) using the strain in wastewater treatment.    USE - The method is used for preparing nitrifying bacteria (claimed).    ADVANTAGE - The method for preparing nitrifying bacteria is simple, easy to perform, low cost and economical.
NOVELTY - Producing ethanol by vapor phase substrate fermentation comprises (a) fermenting synthesis gas containing carbon-monoxide and/or hydrogen gas and microbial culture into a bioreactor to obtain fermentation broth and gas collected from the fermentation broth, (b) separating ethanol and water from the collected gas to obtain fermentation exhaust, (c) enriching carbon monoxide and/or hydrogen gas of fermentation exhaust gas with carbon dioxide of separated fermentation exhaust gas, and (d) reacting fermentation exhaust gas with fresh synthesis gas mixture in the bioreactor to obtain ethanol.    USE - The method is useful for producing ethanol (claimed).    ADVANTAGE - The method improves gas phase substrate conversion rate, increases ethanol production, and reduces energy consumption.
NOVELTY - This utility model claims a kind of marsh gas raw material acidification tank discharging device, comprising a tank and a siphon pipe, water level of the water seal tank is not higher than the acidification tank, and the tank is set on the upper part is connected with the material inlet of the methane tank overflow port, the siphon pipe is bent and one end from the upper part of the acidification tank downwards extends into the bottom, and the other end extends into the bottom of the water seal tank, the siphon pipe bending position is not higher than level of acidification pool predicted raw material storage level. This utility model has simple structure, low manufacturing cost, speed is fast, the production efficiency is high, it is convenient to use, and it is safe and reliable, especially suitable for using animal waste as the raw material marsh gas tank. The animal breeding field, pig farm.
NOVELTY - This utility model claims a kind of marsh gas raw material acidifying pool automatically discharging device, comprising a drainage tube, the inner bottom surface of the acidifying pool is not less than marsh gas pool feeding port, the drainage pipe bending from the upper part of the one end of the acidification tank downwards extends into the bottom, and the other end is connected with the feeding port of the marsh gas tank, the drainage tube bending level is not higher than a acidification tank, predicted raw material storage level. This utility model has simple structure, low manufacturing cost, quick speed, high, convenient to use, safe and reliable, especially suitable for using animal waste as the raw material marsh gas tank. The animal breeding field, pig farm and so on.
NOVELTY - This utility model claims a kind of marsh gas raw material acidification tank anti-blocking discharging device, comprising a drainage tube, the inner bottom surface of the acidifying pool is not less than marsh gas pool feeding port, the drainage pipe bending from the upper part of the one end of the acidification tank downwards extends into the bottom, and the other end is connected with the feeding port of the marsh gas tank, the drainage tube bending level not higher than acidification pool predicted raw material storage level, the drainage pipe bent is provided with drainage hole, the drainage hole is connected with the water injection pipe. This utility model has simple structure, low manufacturing cost, quick speed, high, convenient to use, safe and reliable, especially suitable for using animal waste as the raw material marsh gas tank. The animal breeding field, pig farm.
NOVELTY - This utility model claims a kind of containing microbiological fuel cell of organic sewage treatment device, the microbiological fuel cell comprises at least one anode, a cathode, and an ion exchange membrane of composite electrode, wherein the device comprises a containing groove of the microbiological fuel cell, provided with a water inlet and a water outlet, a temperature control device, a heating device in the temperature control device is connected with the composite electrode between the anode and the cathode of at least one resistance wire, which is set in the groove of the water. The device can be used for processing multiple organic sewage, has the following beneficial effects: it realizes the organic sewage processing temperature is controlled through self capacity, so as to better realize the microorganism to a conversion process, which effectively improves the output power and the COD removing effect.
NOVELTY - This utility model claims a kind of scattered point source sewage processing system, each monomer structure through the UPVC pipe base frame are connected with each other. Each monomer comprises a container of microbial inoculum, the rubber fixing head, sponge column, soft biomass carrier, cladophora oligoclona, plastic net bag, UPVC pipe sealing plug, a rubber fixing head is sleeved on one end of the UPVC pipe and fixed on the bottle container, UPVC pipe is connected with the through hole. container on the rubber fixing head, the other one end of the UPVC pipe is sleeved with soft biomass carrier by UPVC pipe sealing plug, UPVC pipe, UPVC pipe is filled with sponge column, UPVC pipe wall is provided with a drain hole, the soft biomass carrier set is provided with a plastic net bag, soft biomass carrier surface planting cladophora oligoclona, plastic net bag fixing cladophora fascicularis. The structure is simple, the cost is low, the service life is long, the processing effect is good, the whole device is put in water, it does not occupy ground area, the size and flexibly adjust the underwater position, wide use range.
NOVELTY - The utility model claims a marsh gas generating device, especially relates to a kind of rotational flow distributing methane tank. A kind of rotary flow distributing methane tank, comprising a biogas tank body, the top end of the methane tank body middle part is provided with an upper outlet, the upper part of the marsh gas tank body is provided with a feeding pipe and a discharging pipe, the feeding pipe and the discharging pipe is inserted into the marsh gas tank body are located on the same one side of the marsh gas tank body, a feed pipe and a discharge pipe are prefabricated concrete pipe, marsh gas tank body, a feed pipe and a discharge pipe is provided with a rotational flow distributing wall, one side of the rotational flow distributing wall of the marsh gas tank body is connected with the inner wall. This device cancels the discharging passage and lean place of the feeding pipe, the feeding and discharging pipe and a feeding and discharging a prefabricated concrete pipe. The utility model is provided with small floor area, simple structure, pool and low cost.
NOVELTY - The utility model claims a solar auxiliary heating of large biomass pool system, comprising a solar water heater and used for fermentation to generate marsh gas anaerobic digestion tank and solar energy water heater is connected with the water tank, an anaerobic digestion tank is provided with gas-guide tube and a discharging tube, the large biomass pool system further comprises a pre-processing pool, the solar water heater and the pre-processing pool is connected through the water outlet pipe and heat exchange, pre-processing pool, a slurry sedimentation tank and hydrolysis acidification pool, a sedimentation tank, and a hydrolysis acidification pool are provided with pipeline is connected with the water outlet of the solar water heater of the heat exchange tube, the sedimentation tank, a hydrolytic acidification tank and the anaerobic digestion is connected with gas-water separator of the anaerobic digestion tank, slag of the anaerobic digestion pool is connected to the sedimentation tank. Solar water heater used in winter to compensate the temperature of the yeast slurry sedimentation tank and hydrolysis acidification pool, which is good for improving marsh gas generating rate.
NOVELTY - The utility model claims a marsh gas anaerobic digestion tank, comprising a fermentation tank body, the tank body is provided with marsh gas feeding pipe, an air guide pipe and a discharging pipe, gas-guide tube and the gas-water separator is connected with the tank body, a slag tank body is connected to the sedimentation tank, the marsh gas anaerobic digestion pool further comprises a solar water heater and a water tank, wherein the solar water heater is connected with the water tank through the pipeline, the solar water heater and the tank body are connected with each other through a water pipe and a heat exchanger, wherein the tank body is connected with the water outlet pipeline of the solar water heater of the heat exchange tube. Using the device to dairy manure and so on to marsh gas ferment, temperature of the marsh gas tank is improved, is increased.
NOVELTY - Pseudomonas aeruginosa lipase gene (I) having a sequence of SEQ ID NO: 1 (a 2134 base pair sequence fully defined in the specification), is new.    USE - (I) is useful for producing biodiesel, as a feed additive and for the preparation of substances for the metabolism of fatty acids (all claimed).    ADVANTAGE - (I) has high hydrolyzing activity and transesterification activity, produces high content of biological diesel oil with good quality, and can improve chicken weight, reduce material meat ratio of chicken and reduce the feeding cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) lipase protein having a sequence of SEQ ID NO: 2 (a 610 amino acid sequence fully defined in the specification) of the polypeptide comprising the gene; and    (2) a transformed host cell comprising the lipase gene, where the cell is original nucleated cells or eukaryotic cells.
NOVELTY - Pre-processing crop straw from heat storage medium comprises fruit harvesting or fruit harvesting after 24 hours; straw crushing; and carrying out heating, where the moisture of the straw is reduced to less than 11 wt.%.    USE - The method is useful for pre-processing crop straw from heat storage medium (claimed).    ADVANTAGE - The method improves the accessibility of the cellulose in the straw cellulose by microorganism. It can reduce the cost and improve the utilization rate of straw. The nutrition value is improved.
NOVELTY - Preparing preservative comprises mixing 30-150 pts. wt. of sugar, 3-4 pts. wt. of urea, 30-50 pts. wt. of potassium dihydrogen phosphate, 1500-2000 pts. wt. of water, 0.1-0.2 pts. wt. of silver nitrate and 0.1-0.2 pts. wt. of 8-hydroxyquinoline sulfate, and dissolving 8-hydroxyquinoline sulfate in water.    USE - The method is useful for preparing preservative (claimed).    ADVANTAGE - The method is capable of easily and economically preparing the preservative in an eco-friendly manner without peculiar smell.
NOVELTY - This utility model claims one kind of marsh gas desulphurization tank, comprising a tank body, the air inlet pipe, an air outlet pipe, a supporting plate, a feed pipe, a discharge pipe and a water outlet, said upper and lower ends of the tank body are respectively provided with an air outlet pipe and an air inlet pipe, said tank top is provided with a feeding pipe, the top side is further provided with a discharging opening, said tank body bottom is provided with a supporting plate, said supporting plate is just completely covers the section's said tank body, said supporting plate is a hole-shaped air inlet pipe, a discharge pipe and lower part of supporting plate is covered on the surface one-layer quartz sand, said quartz sand surface layer is covered, bottom end of said tank body is provided with a water outlet. The utility model is provided with feeding port and marsh gas desulphurization tank is set on the top side of the discharge hole, it can through the discharging port in real time using condition's desulfurizing agent in the tank, taking the proper's change, the marsh gas supply's; the hole plate paved at the same time also can be quartz sand so as to remove target's water.
NOVELTY - Garbage carbonization pyrolysis furnace, belonging to the technical field of environment-friendly device. One vertical furnace body upper part is feeding port, a slag outlet is set at the bottom, a furnace body is further provided with a smoke outlet, wherein the furnace body two sides of the lower side is fastened with a plurality of magnetic core is composed of a top to bottom parallel arranged at intervals form's's magnetic core assembly, is provided with an air inlet part of the interval's plurality of core. Advantages: because the air inlet is set on a plurality of magnetic core's interval part, so the furnace's air must be through magnetic core assembly in the air oxygen atom by the action's magnetic field is strong, the oxygen atom active high magnetic field atom fluctuation effect is obvious, the carbide furnace cracking ability's garbage is further improved.
NOVELTY - The utility model claims a biomass fuel particle production, belonging to the technical field by using waste fungus bag for processing biomass fuel particle's production line, comprising in turn connecting's raw material crushing device, drying device and granulating device and cooling device, said raw material crushing device by the conveyor connecting the drying device and drying device in turn connecting belt conveyor, a lifter, a lifting connecting granulating device, granulating device through the belt conveyor, bucket elevator connecting cooling device, the cooling device is hoisting machine connecting the finished product. This utility model is rational in structure and design, the property's waste fungus bag contents are connecting set crushing, drying, granulating and cooling device, the operation process is clear, obviously improve the particle processing efficiency and improve the energy utilization rate, avoid raising dust in production process's environment's pollution production biomass particle grading package's, the economic benefit and social benefit are very ideal, and has very good's industrial production application value.
NOVELTY - This utility model said biological particle's type and fixed annealing furnace belongs to the technical field of combustion furnace, furnace material distribution device and automatic power distribution box is composed of a combustion furnace material distribution device is set in said combustion furnace is provided with a combustion chamber and the annealing chamber, the combustion chamber material distribution device is set on the one side of the annealing chamber is set in the middle position in the combustion furnace, the combustion chamber and the annealing chamber is provided with a flame channel, said annealing chamber is provided with an air outlet pipe, the bottom is provided with a moving car, the upper is provided with a thermoelectric couple, said outlet pipe is provided with the combustion chamber part, hot-water outlet pipe extends upwards combustion furnace. The utility model has following beneficial effects:'s to renewable biomass particle fuel, it has high automatic degree, high furnace temperature uniformity, the temperature in the furnace between 0-1200 degrees C, the production efficiency is high, the low-carbon environment-friendly, simple in structure, safe and reliable operation, low operation cost and so on, replacing fuel oil, fuel gas, coke, optimal product's electric furnace.
NOVELTY - The utility model claims full-automatic biological particle inlet tube annealing furnace belongs to the technical field of stove, comprising a combustion furnace, a material distribution device and automatic power distribution box is composed of a combustion furnace material distribution device is set in said combustion furnace is provided with a combustion chamber, the combustion temperature in the furnace is 0-1200 degrees C, burning furnace middle part is set with the roller, two ends of the roller bearing base on the upper middle passes through the combustion chamber, one end is provided with a gear, and the gear is driven to rotate, said combustion chamber is provided with a thermoelectric couple and lift. The utility model has following beneficial effects:'s to renewable biomass particle fuel, it has high automatic degree, furnace temperature uniformity, combustion temperature in the furnace is between 0-1200 degrees C, the production efficiency is high, the low-carbon environment-friendly, simple in structure, safe and reliable operation, low operation cost and so on, replacing fuel oil, fuel gas, coke, optimal product's electric furnace, it can help the enterprise's energy consumption cost is reduced by 30-60 %, the saves the non-renewable resources.
NOVELTY - The utility model claims one for biological fertilizer production's intelligent control system, comprising a control unit, a control unit and a first programmable controller, a second programmable controller and the programmable controller is connected with the first programmable controller is connected with a spraying liquid level control device, and control device, the material transfer control device and fermentation control device connected with the second programmable controller is connected with the material filling control device, the third programmable controller is connected with the sewage processing device is connected, a liquid level control device and the ultrasonic wave sensor and the sewage pump, and control device and turning machine, material transfer control device is connected with the transmission belt, the fermentation control device is connected with the temperature sensor. The utility model has following beneficial effects: the raw material's , after fumigation transfer to the fermentation workshop taking fermentation sterilizing, at last, automatic filling, the sewage in the production processing's discharge and protects the environment, has simple structure, is convenient to use, has no pollution to the environment and so on.
NOVELTY - The system has a biogas system, system for aquiculture, planting system and stock-raising system that are connected together. The planting system and the stock-raising system are connected with the biogas system. The biogas system is provided with a biogas tank and biogas power generation unit.    USE - Synthetic agricultural system used in aquaculture industry for planting grass and corn, and for feeding pig, cattle, chicken, duck and edible fish.    ADVANTAGE - The synthetic agricultural system is more efficient, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the synthetic agricultural system. (Drawing includes non-English language text)
NOVELTY - The device has a single chip microcomputer connected with a digital display module. An acousto-optic alarm module and a pre-positive circuit module are connected with a front circuit module that is connected with a methane detecting module. A carbon monoxide detecting module is connected with a stabilizing circuit module that is connected with a battery module. The battery module is connected to the front circuit module. The single chip micro-computer is provided with an under-voltage shutdown module. The carbon monoxide detecting module is provided with a carbon monoxide sensor.    USE - Wearable methane carbon monoxide measuring device.    ADVANTAGE - The device is convenient to carry and maintain, and occupies less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a wearable methane carbon monoxide measuring device.'(Drawing includes non-English language text)'
NOVELTY - Crucian feed comprises 10-20 wt.% fishmeal, 30-45 wt.% soybean meal, 3-10 wt.% corn flour, 1-6 wt.% wheat flour, 30-40 wt.% wheat bran, 0.5-2 wt.% mineral mixture, 0.1-1 wt.% vitamin mixture, and 0.5-2 wt.% Chinese herbal medicine.    USE - The crucian feed is useful for increasing disease resistant in crucian.    ADVANTAGE - The crucian feed is prepared by simple method, rich in protein, vitamin and mineral substance, and environmentally-friendly.
NOVELTY - The system has an upper vacuum pump that is provided with an intelligent control rotary reaction kettle which is connected with a vacuum suction pipe. Temperature sensor and humidity sensor are arranged for detecting the temperature and humidity of vacuum rotary reaction kettle. An intelligent control centre is arranged for controlling the vacuum pump to work in specific temperature and humidity of vacuum rotary reaction kettle.    USE - System for preparing fuel from waste in agricultural field and forestry field.    ADVANTAGE - Since the intelligent control centre is arranged for controlling vacuum pump to work in specific temperature and humidity of vacuum rotary reaction kettle, the fuel can be manufactured efficiently from waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel preparing system.
NOVELTY - Butane-air mixing distributor comprises a collecting pipe (5), a distributing pipe (6) and a mixing tube (9). The distribution pipe is vertically connected with the collecting pipe. The distributing pipe is inserted into the mixing tube. The insertion direction of the distributing pipe is vertical to the axis of the mixing pipe diameter. A welding pipe is corresponding to the inner mixing tube and the distributing pipe. The distributing pipe is provided with a blocking plate, an inserting tube (8) and multiple exhaust holes (7) at its upper end.    USE - Used as butane-air mixing distributor.    ADVANTAGE - The device: reduces explosive gas volume; improves the mixing uniformity of the raw material gas; uniformly carries out gas-solid reaction, which is good for prolonging the service life of the catalyst; and improves the production safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the butane-air mixing distributor.    Collecting pipe (5)    Distributing pipe (6)    Exhaust holes (7)    Inserting tube (8)    Mixing tube (9)
NOVELTY - A sodium carboxymethyl cellulose-pretreatment wastewater is provided to a conditioning tank. The water is provided to corrosion-resistant injection anaerobic-sequencing-batch-reactor (ASBR) reaction cell and processed. The wastewater is provided to pool for biochemical reaction, mechanical stirred and natural precipitated. The supernatant after precipitation is provided to aerobic depth processing unit. The sludge in settling tank and anaerobic-sequencing-batch reactor is provided to sludge thickener and filter-pressed. The supernatant is refluxed and press-filtrated.    USE - Method for treating sodium carboxymethyl cellulose-pretreatment wastewater (claimed).    ADVANTAGE - The method reduces chemical oxygen demand in sodium carboxymethyl cellulose-pretreatment wastewater, efficiently recovers biogas, and improves biodegradability of wastewater.    DETAILED DESCRIPTION - A sodium carboxymethyl cellulose-pretreatment wastewater is provided to a conditioning tank, and water quality is regulated. The water is provided to corrosion-resistant injection anaerobic-sequencing-batch-reactor (ASBR) reaction cell and processed for predetermined time, and pumped. The pumped wastewater is provided to pool for biochemical reaction in anaerobic-sequencing-batch reactor provided with electric submersible mixer at bottom, mechanical stirred and natural precipitated. The supernatant after precipitation is provided to aerobic depth processing unit via gravity decanter, and the water level in pool is set and decanter is drained. The sludge in settling tank and anaerobic-sequencing-batch reactor is provided to sludge thickener, filter press, dewatered and concentrated in pool. The supernatant is refluxed and press-filtrated.
NOVELTY - Removal of nitrogen and phosphorus in biogas slurry involves adding mixture of activated carbon and scrap iron to biogas slurry, adjusting the pH value of the biogas slurry to 4-5, aerating, feeding the resultant slurry into micro-electrolysis reactor, performing micro-electrolysis reaction, adjusting pH value to 4-5, introducing the resultant reaction liquid into serially-connected water electrolytic reactor, performing water electrolytic reaction, adjusting the pH value of the resultant liquid to 8.5-9.5, maintaining for 30 minutes, removing the supernatant, sampling and detecting.    USE - Removal of nitrogen and phosphorus in biogas slurry (claimed).    ADVANTAGE - The method efficiently enables the removal of nitrogen and phosphorus in biogas slurry with high removal rate of nitrogen and phosphorus, by a simple process.    DETAILED DESCRIPTION - Removal of nitrogen and phosphorus in biogas slurry involves adding mixture of activated carbon and scrap iron in volume ratio of 1:1-3:1, to biogas slurry, adjusting the pH value of the biogas slurry to 4-5, aerating for 1.5-4 hours in aeration rate of 6 L/minute.L, feeding the resultant slurry into three serially-connected micro-electrolysis reactor, performing micro-electrolysis reaction for 2.5 hours in rate of 6 L/minute.L, adjusting pH value to 4-5, introducing the resultant reaction liquid into serially-connected water electrolytic reactor, performing water electrolytic reaction for 2.5 hours in rate of 3.5 L/minute.L, adjusting the pH value of the resultant liquid to 8.5-9.5, maintaining for 30 minutes, removing the supernatant, sampling and detecting. The volume ratio of biogas slurry, activated carbon and scrap iron is 4:3-7:3.
NOVELTY - An organic selenium fertilizer comprises 400-500 pts. wt. chicken manure, 30-50 pts. wt. spinach residue leaf, 80-120 pts. wt. bean straw, 50-80 pts. wt. corn kernels corn cob, 40-60 pts. wt. kieselguhr, 10-30 pts. wt. radix astragali powder, and 80-120 pts. wt. sweet potato rice.    USE - An organic selenium fertilizer.    ADVANTAGE - The fertilizer improves soil selenium content, and improves crop absorption rate.
NOVELTY - A temperature-controlled double cylindrical aerobic compost reactor comprises small cylinder (2) and a large cylinder (1). The top part of the large cylinder is provided with a large top cover (11). The large top cover is provided with upper outer air-through pipe socket (14), an outer air outlet (12), an outer thermometer faucet (15) and the sampling hole (13). An air-through pipe socket (24) is located in the small cylinder. The inner cavity of the air-through pipe lower end connects with gas distribution pipe (8).    USE - A temperature-controlled double cylindrical aerobic compost reactor.    DETAILED DESCRIPTION - A temperature-controlled double cylindrical aerobic compost reactor comprises small cylinder (2) and a large cylinder (1). The small cylinder is placed in large cylinder inner cavity. The top part of the large cylinder is provided with a large top cover (11). The large top cover is provided with upper outer air-through pipe socket (14), an outer air outlet (12), an outer thermometer faucet (15) and the sampling hole (13). An outer water outlet is provided on the large upper cylinder sidewall. The top part of the small cylinder is provided with a small top cover. The inner cavity interlayer is provided with upper layer air-through pipe socket and interlayer ventilation holes. A lower end air-through pipe passes through the outer air-through pipe socket. An air-through pipe socket (24) is located in the small cylinder. The inner cavity of the air-through pipe lower end connects with gas distribution pipe (8).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the temperature-controlled double cylindrical aerobic compost reactor.    Cylinders (1, 2)    Gas distribution pipe (8)    Outer air outlet (12)    Sampling hole (13)    Upper outer air-through pipe socket (14)    Outer thermometer faucet (15)    Air-through pipe socket (24)
NOVELTY - A soilless culture organic release fertilizer comprises 20-50% chicken manure, 30-60% cake fertilizer, 3-5% hyaluronic acid, 3-5% bran, 4-5% powdered rock phosphate, and 4-5% mineral potassium fertilizer.    USE - A soilless culture organic release fertilizer.    ADVANTAGE - The fertilizer has reduced production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soilless culture organic release fertilizer comprising:    (A) drying chicken manure to make the water content reach 20-30%, putting the prepared cake fertilizer, humic acid fertilizer, and bran, crushed rock and mineral potassium fertilizer into a fermenting tank;    (B) adding 40-60% water, taking normal temperature for 3-7 days, controlling the fermentation tank at 50-65 degrees C, mechanical blowing and stirring the fermented mixed material; and    (C) drying at 30-50 degrees C to make the water content to 12-15%, granulating and coating.
NOVELTY - A Ganoderma lucidum cultivating material comprises 10-16 wt.% walnut branch meal, 20-24 wt.% shell meal, 25-35 wt.% nutshell crumbs, 16 wt.% cotton seed hull, 12 wt.% bran, 5 wt.% soybean powder, 1 wt.% calcium superphosphate, and 1 wt.% light calcium carbonate.    USE - Ganoderma lucidum cultivating material.    ADVANTAGE - The material degrades toxic bacteria, promotes the growth of lucid ganoderma mycelium, has good ventilation property and water-retaining property, and provides high yield with biological efficiency of 12.5%-14%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the cultivating material.
NOVELTY - A fertilizer is prepared by crushing corn cob, bean, and corn straw to 100-120 meshes; taking pig dung, duck dung, clover, tobacco rod and tobacco leaf fertilizer, corn cob, sludge, golden cypress powder and corn kernel into fermentation tank, adding water to immerse the material, and fermenting for 25-30 days; and adding with selenium and sodium selenite, stirring them uniformly, drying until water content is 45-55%, stirring uniformly, adding microelement, taking into extruder, and extruding and granulating.    USE - Method for manufacturing fertilizer for enhancing selenium absorption rate of crops (claimed).    ADVANTAGE - The method is simple, and provides fertilizer with high content of selenium.
NOVELTY - A fertilizer is prepared by taking vermiculite, chicken manure, cow dung, yellow mealworm, straw powder, bone powder, trace element, bentonite, limestone, and ammonia water; crushing vermiculite and limestone into 80-120 meshes powder, heating to 150-200 degrees C for 4 hours, and cooling to room temperature; fermenting chicken manure, cow dung, yellow mealworm, straw powder, and bone meal for 15-18 days; mixing the obtained mixtures, adding trace elements, bentonite and water, adding ammonia water, and detecting water content of 52-55%; and taking the mixture into granulating machine, and drying.    USE - Method for preparing fertilizer for promoting root growth (claimed).    ADVANTAGE - The method is simple and convenient.
NOVELTY - A fertilizer comprises 400-500 pts. wt. pig manure and duck manure mixture, 30-50 pts. wt. clover, 80-120 pts. wt. tobacco stalk and tobacco leaf fertilizer, 50-80 pts. wt. corn cob, 40-60 pts. wt. silt, 10-30 pts. wt. golden cypress powder, and 80-120 shell powder.    USE - Fertilizer for enhancing selenium absorption rate of crop (claimed).    ADVANTAGE - The fertilizer increases crop selenium absorption rate by 35%, compared with traditional fertilizer which is only 18-22%.
NOVELTY - A selenium-containing organic fertilizer is prepared by crushing corn kernel, sweet potato, and bean straw to 100-120 meshes; taking chicken manure, spinach leaf residue, bean straw, corn kernel, diatomite, radix astragali powder, and sweet potato into fermentation tank, adding water immerse the material, and fermenting for 25-30 days; and adding selenium and sodium selenite, stirring them uniformly, drying until water content is 45-55%, stirring uniformly, adding microelement, and extruding and granulating.    USE - Method for preparing selenium-containing organic fertilizer (claimed).    ADVANTAGE - The method is simple and provides organic fertilizer having high content of selenium.
NOVELTY - A fertilizer is prepared by taking radix bupleuri, duck manure, cow manure, yellow mealworm, seaweed, food residue, microelement, river sludge, calamine, and urea; crushing calamine into 80-120 meshes powder, heating to 150-200 degrees C for 4 hours, and cooling to room temperature; fermenting duck manure, cow manure, yellow mealworm, seaweed, and food residue mixture for 15-18 days; mixing the obtained mixtures, adding microelement, river sludge and urea, adding water, and detecting water content of 52-55%; and granulating the mixture, and drying.    USE - Method for preparing fertilizer for promoting root growth of seedling (claimed).    ADVANTAGE - The method is simple.
NOVELTY - A fertilizer for improving lean soil is prepared by crushing corn cob, purple sweet potato, and bean type straw to 100-120 meshes; fermenting chicken manure, duck manure, food debris, corn cob, bentonite, radix scutellariae powder, and corn kernel for 25-30 days; and adding selenium and sodium selenite, stirring them uniformly, drying until water content is 45-55%, stirring uniformly, adding microelement, and extruding and granulating.    USE - Method for preparing fertilizer for improving lean soil (claimed).    ADVANTAGE - The method is simple, and provides organic fertilizer having high content of selenium.
NOVELTY - A fertilizer comprises 1-1.5 pts. wt. fermented manure, 0.8-1.5 pts. wt. honey, 0.4-0.6 pts. wt. high-potassium type fertilizer, and 280-320 pts. wt. water. The fermented manure comprises biogas slurry. The fertilizer is prepared by weighing 40-60 pts. wt. phosphate fertilizers, 30-40 pts. wt. peanut bran, and 120-150 pts. wt. water, uniformly mixing, fermenting for 1-5 months, filtering, and collecting filtrate.    USE - Fertilizer for fruit or vegetable (claimed).    ADVANTAGE - The fertilizer increases yield by 20-25%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer.
NOVELTY - A red mushroom cultivating material comprises 8-12 wt.% walnut branch meal, 16-22 wt.% shell meal, 28-38 wt.% nutshell crumbs, 18 wt.% cotton seed hull, 15 wt.% rice bran, 3 wt.% bean cake, 1 wt.% calcium superphosphate, and 1 wt.% gypsum powder.    USE - Red mushroom cultivating material.    ADVANTAGE - The material degrades toxic bacteria, promotes growth of red mushroom, has good ventilation property, and provides high yield with biological efficiency of 128.5-135%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the cultivating material.
NOVELTY - An abalone mushroom cultivating material comprises 8-12 wt.% walnut branch meal, 15-21 wt.% shell meal, 25-35 wt.% nutshell crumbs, 20 wt.% corn cob, 15 wt.% bran, 5 wt.% corn powder, 1 wt.% calcium superphosphate, and 1 wt.% gypsum powder.    USE - Abalone mushroom cultivating material.    ADVANTAGE - The material degrades toxic bacteria, promotes abalone mushroom growth, has good ventilation property and water-retaining property, and provides high yield with biological efficiency of 96.8-112.3%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the cultivating material.
NOVELTY - An organic fertilizer comprises 50-70 wt.% livestock manure, 5-15 wt.% tobacco residue, 2-8 wt.% rice bran, 2-8 wt.% straw powder or grass powder, 5-15 wt.% bone residue, 12 wt.% shell powder, 0.1-0.13 wt.% bacillus licheniformis and 0.1-0.13 wt.% functional strain.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer has scientific formulation, has high nutrient and resists pest and disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising mixing livestock manure, tobacco residue, rice bran, straw powder or grass powder, bone residue, shell powder and bacillus licheniformis, stirring, aerobic fermenting at 70 degrees C for less than or equal to 4-6 days, adding functional strain, fermenting for 7-8 days, decomposing to obtain mixture 2, storing, secondary fermenting, removing impurities, and drying or granulating.
NOVELTY - A cationic organic fertilizer comprises 5-10 pts. wt. cation exchange resin, 10-20 pts. wt. red bean, 10-20 pts. wt. crown flower, 40-50 pts. wt. cow manure, 30-50 pts. wt. straw powder, 1-2 pts. wt. phosphate and potassium solubilizing bacteria, 2-4 pts. wt. polyvinyl alcohol and 1-2 pts. wt. fermenting bacteria.    USE - Cationic organic fertilizer.    ADVANTAGE - The fertilizer has improved saline-alkali effect.
NOVELTY - A rubber vulcanization accelerator N,N'-dicyclohexyl-2- benzothiazole sulfenamide is prepared by mixing sulfuric acid, hydrogen peroxide and water with 1: 2.5-2.7:9 mole ratio, adding oxidant with 1-2:2-3 weight ratio, adjusting to pH 12 with sodium hydroxide, adding isopropanol with 10-12:1 mole ratio, reacting with secondary amine cyclohexane and isopropyl alcohol at 30-80 degrees C, mixing at 500-1200 revolutions/minute, adding 85-90% accelerating agent, stirring for 2-3 hours, adjusting to pH 9-11, filtering, washing with water, and drying.    USE - Method for preparing rubber vulcanization accelerator N,N'-dicyclohexyl-2-benzothiazole sulfenamide (claimed).    ADVANTAGE - The method has simple operation, environment-friendly effect, and 85% yield of 98% pure product.
NOVELTY - A plant-derived parthenolide compound is prepared by drying leaves, pulverizing, sieving, extracting with supercritical carbon dioxide for 3-5 hours, setting extraction cylinder to 35-45 degrees C under 15-20 MPa pressure, isolation cylinder to 50-60 degrees C under 10-15 MPa pressure and separation cylinder to 40-50 degrees C under 4-8 MPa pressure, discharging extracted solution, mixing with silica gel, performing column chromatography, rinsing, collecting, and recrystallizing.    USE - Method for preparing plant-derived parthenolide compound (claimed).    ADVANTAGE - The method is simple and has high yield.
NOVELTY - Garbage processing device comprises garbage heating device and gas purifying device. Heating device comprises first heating cavity and second heating cavity. First heating chamber and second heating chamber are connected form a sealed cavity space. Acidic gas is produced by rapid heating in first heating cavity, where acid gas is purified by purifying device and then cracking is performed. The gas is then subjected to high temperature continuously in the second heating cavity.    USE - Garbage processing device.
NOVELTY - The device has a main structure that is provided with upper heating cavity (103) and lower heating cavity (105). The upper and lower heating cavities are provided with upper heating ring (1035) and lower heating ring (1055), respectively. The heating temperature of upper heating cavity is 90-500 degrees centigrade. The heating temperature of lower heating cavity is 180-800 degrees centigrade.    USE - Device for processing household garbage.    ADVANTAGE - The device can prevent the leakage of internal reaction combustible gas so as to avoid fire or explosion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the household garbage processing device.    Upper heating cavity (103)    Lower heating cavity (105)    Carbon activating device (109)    Upper heating ring (1035)    Lower heating ring (1055)
NOVELTY - Aqueous liquid fuel comprises methanol, water, aliphatic hydrocarbon and preservative in mass ratios of 95-99, 95-99, 3-10, 2-5 and 0.01-0.05 respectively. Boiling point range is 15-100 degrees C, and research octane number of fuel is 85-95.    USE - Aqueous liquid fuel used in combustion engine (claimed), for preventing corrosion of metal, engine oil system and oil pipe.    ADVANTAGE - The aqueous liquid fuel is eco-friendly, good ignition efficiency and prevention of corrosion in an economic manner.
NOVELTY - Aqueous liquid fuel composition comprises (in pts.wt.): methanol (30-60), water (15-30), propylene glycol (15-30), potassium hydroxide (0.5), dicyclopentadienyl iron (0.1) and solvent oil (3).    USE - Aqueous liquid fuel composition for providing regenerative high temperature air combustion (claimed).    ADVANTAGE - The aqueous liquid fuel composition is cost-effective and reduces production of mono-nitrogen oxide (nitric oxide and nitrogen dioxide) and toxic substances.
NOVELTY - Oxygen-enriched aqueous liquid fuel composition comprises (in wt.): methanol (70-95), water (3-10), potassium hydroxide (0.01-0.08), sodium hydroxide (0.01-0.08), Dess-Martin reagent (0.1-1), solvent oil (10-28), potassium permanganate (0.01-0.05) and potassium chloride (0.01-0.08).    USE - Oxygen-enriched aqueous liquid fuel composition used in all kinds of stove.    ADVANTAGE - The oxygen-enriched aqueous liquid fuel composition ensures cost-effective and has wide application in burner requiring less oxygen demand.
NOVELTY - Aqueous liquid fuel comprises (in pts.wt.): purified water (3-15), methanol (70-90), n-butyl alcohol (3-5), Dess-Martin reagent (0.1-1), alcohol (0.1-0.5), glycerin (0.1-0.5) and thiol compound (0.0002-0.0008).    USE - Aqueous liquid fuel used for industrial spray combustion (claimed).    ADVANTAGE - The aqueous liquid fuel is eco-friendly, safe and cost-effective, ensures improved combustion up to 9200 kilocalorie/kg, and has low volatility and stable combustion properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing aqueous liquid fuel, which involves:    (A) adding pure water, methanol, n-butyl alcohol, Dess-Martin reagent and glycerol in a reaction kettle at normal temperature with continuous stirring for 5-15 minutes to obtain mixed solution;    (B) keeping obtained mixed solution for 0.5 hours;    (C) adding preservative, alcohol and thiol compound with the obtained solution with continuous stirring for 10-15 minutes to obtain product;    (D) keeping obtained product at normal temperature; and    (E) sealing obtained product to obtain the desired product.
NOVELTY - Optimizing thermal performance of refuse derived fuel involves selecting initial garbage with less than 30 wt.% of water content and then adding 5-15 wt.% of wetting agent to the initial garbage. The obtained material is uniformly stirred and then the obtained stirred material is dried for 1-2 days. The obtained dried material is added with combustible solid and combustion improver, where quantity of combustible solid is 10-20 wt.% and of combustion improver is 0.5-1 wt.% of initial mass of garbage. The obtained material is uniformly mixed to obtain refuse derived fuel.    USE - Method for optimizing thermal performance of refuse derived fuel.    ADVANTAGE - The method enables to optimize thermal performance of refuse derived fuel in a cost-effective manner, and fulfills demand to replace fossil fuel.
NOVELTY - The water electrolyzer has a separator set with a gas cooler. The hydrogen-oxygen washer main body has a washing cabin (3) containing electrolyzed water, the cabin provided with an air inlet pipe (5) at the upper side wall. One end of the air inlet pipe is connected with the exhaust port of the separator, while the other end extends into the water. The cabin is also provided with a gas outlet (6), and a separator at the side wall.    USE - Water electrolyzer for hydrogen peroxide scrubber.    ADVANTAGE - Reduces the alkali level in the finished product, while enabling the repeated use of the recycled alkali, thus reducing operation costs. Reduces gas temperature, thus reducing the load on the gas cooler to in turn reduce temperature and humidity of the produced gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structural diagram of the water electrolyzer.    Nozzle plate assembly (2)    Washing cabin (3)    Overflow port (4)    Air inlet pipe (5)    Gas outlet (6)
NOVELTY - Disc plant fertilizer plant comprises 40-50 pts. wt. ammonium nitrate, 20-25 pts. wt. ammonium phosphate, 20-30 pts. wt. potassium nitrate, 5-10 pts. wt. ammonium chloride, 6-11 pts. wt. calcium sulfate, 1-2 pts. wt. ferrous sulfate, and 1-2 pts. wt. copper sulfate.    USE - Disc plant fertilizer plant.    ADVANTAGE - The fertilizer is low cost, green and environment-friendly, and convenient to use.
NOVELTY - Ethane and propane are prepared from synthesis gas by performing single-step conversion to synthesis gas in the presence of multifunctional composite catalyst in which composite catalyst is obtained by mixing carbon monoxide (CO) hydrogenation catalyst as 1st catalyst component and metal-modified molecular sieve as 2nd catalyst component with mass ratio of 10:1-1:10, preferably 3:1-1:3.    USE - Preparation of ethane and propane from synthesis gas (claimed).    ADVANTAGE - Preparation method has ethane and propane total selectivity in hydrocarbon of greater than or equal to 70% and methane selectivity in hydrocarbon of greater than or equal to 5%, improves CO conversion rate, and reduces device investment, energy consumption, operation cost, and by-products.
NOVELTY - Alverine citrate is synthesized by reacting 3-halophenyl propane and ethylenediamine hydrochloride to obtain diphenyl propylamine, reacting with alkali solution and reacting with citric acid.    USE - Synthesis of alverine citrate (claimed).    ADVANTAGE - The synthesis method is simple, environment-friendly, uses mild reaction conditions, and has high production yield.
NOVELTY - Isopropyl hydrazine derivative is prepared by reacting 2-substituted isopropane compound with carbazate compound in presence of organic solvent and inorganic or organic base.    USE - Preparation of isopropyl hydrazine derivative for preparing pharmaceutical intermediates.    ADVANTAGE - Preparation of isopropyl hydrazine derivative has low raw material cost and does not use high-pressure hydrogenation reaction or heavy metal catalyst.    DETAILED DESCRIPTION - Isopropyl hydrazine derivative of formula (III) is prepared by reacting 2-substituted isopropane compound of formula (I) with carbazate compound of formula (I) in presence of organic solvent and inorganic or organic base.    R=Me, Et, or alkyl, preferably Me or Et; and    X=Br, I, Cl, methanesulfonate, or OTs, preferably Br and OTs.
NOVELTY - A 2,3-dichloro-5-methyl pyridine is synthesized by mixing N-propyl-benzylamine, chloracetyl chloride, and trimethylamine, triethylamine, tripropylamine, pyridine, 3-methyl pyrazole, or potassium carbonate acid-binding agent at molar ratio N-propyl-benzylamine:chloracetyl chloride:acid-binding agent of 1:05-2:0.5-2, reacting by acylation reaction at - 10-60 degrees C to obtain N-benzyl-N-propenyl- alpha -chloroacetamide, adding with dimethyl ammonium chloride at molar ratio N-benzyl-N-propenyl- alpha -chloroacetamide:dimethyl ammonium chloride of 1:1-2 at 20-120 degrees C, and reacting by cyclization reaction.    USE - Preparation of 2,3-dichloro-5-methyl pyridine for pesticides.    ADVANTAGE - The method is environment-friendly, and low cost, has high yield, mild reaction condition, and high industrial value.
NOVELTY - Preparing clopidogrel and its intermediates involves: (1) reacting thionyl chloride and ortho chlorobenzene glycin with methanol; (2) using L-(+)-tartaric acid to the ortho chlorobenzene glycin methyl ester; (3) obtaining 2-2-thiophene-ethyl amino acid methyl ester hydrochloride and organic solvent by using S -(+) methyl ester ortho chlorobenzene glycin L-(+)-tartrate and 2-(2) ethanol p-toluene sulfonate under the alkaline condition; and (4) cyclization reaction of 2-chlorophenyl -2-thiofuran ethyl amino acid methyl ester hydrochloride and formaldehyde.    USE - The method is useful for preparing clopidogrel and its intermediates (claimed).    ADVANTAGE - The method is simple, the yield is high, the cost is low, and the operation is simple. The method has no special toxic and harmful reagent, which is good for normal pressure operation. It is environment-friendly, and the reaction condition is mild.    DETAILED DESCRIPTION - Preparing clopidogrel and its intermediates involves: (1) reacting thionyl chloride and ortho chlorobenzene glycin with methanol to obtain o-fluorobenzene glycine acid methyl ester; (2) using L-(+)-tartaric acid to the ortho chlorobenzene glycin methyl ester, taking S-(+) methyl ester ortho chlorobenzene glycin L-(+)-tartrate salt crude product, refining to obtain S-(+) methyl ester ortho chlorobenzene glycin L-(+)-tartrate; (3) obtaining 2-2-thiophene-ethyl amino acid methyl ester hydrochloride and organic solvent by using S -(+) methyl ester ortho chlorobenzene glycin L-(+)-tartrate and 2-(2) ethanol p-toluene sulfonate under the alkaline condition; and (4) cyclization reaction of 2-chlorophenyl -2-thiofuran ethyl amino acid methyl ester hydrochloride and formaldehyde to obtain clopidogrel, then in the organic solvent, reacting with sulfuric acid to generate clopidogrel hydrogen sulfate.
NOVELTY - A soilless culture nutrient material comprises 237-280 pts. wt. ammonium sulfate, 537-580 pts. wt. magnesium sulfate, 126-170 pts. wt. calcium nitrate, 250-290 pts. wt. potassium sulfate, 350-390 pts. wt. potassium chloride, 10-15 pts. wt. ferric sulfate, 3-8 pts. wt. borax, 4-6 pts. wt. manganese sulfate, 1-3 pts. wt. sodium molybdate, 1-3 pts. wt. zinc sulfate, and 1-3 pts. wt. copper sulfate.    USE - A soilless culture nutrient material used for green vegetable (claimed).    ADVANTAGE - The soilless culture nutrient material uses easy to obtain raw material, is inexpensive and convenient to use, and is environment-friendly.
NOVELTY - The utility model claims one water for preparing standard gas instrument. A water one standard gas generating device, an electrolytic tank and the converter connecting the front connecting with a humidity generator electrolytic cell, the electrolytic cell after connecting with a switch valve and molecular sieve dehydrator. The front humidity generator connecting with a mass flow meter. Bottled high pressure carrier gas after connecting row-washing type pressure regulator. Around the electrolytic cell is type or externally wound type, electrolyte is phosphoric acid solution. After converter connecting with an adjusting valve and a switch valve. Switch valve and switch valve dehydrator after converter, does not need the water standard time are in the closed state. 's working principle is as follows: the instrument high temperature copper oxide in the converter to electrolysis to generate hydrogen reaction to generate the hydrogen is equal to molar weight water to make the carrier gas in the scalar water standard. The instrument generating scalar water is simple, fast, accurate and reliable. Gas content, output pressure and output flow rate within a predetermined range, it can be adjusted at random, application range is wide.
NOVELTY - The method comprises performing hydrothermal carbonization on a raw material with catalyst and then filtering to obtain solid fuel. The step of performing hydrothermal carbonization comprises mixing the raw material with 50-95% of hot water, and is carried out at 210-250 degrees C, preferably 220-245 degrees C for 0.1-1 hour. The raw material is wood-based biomass.    USE - The method is useful for producing solid fuel (claimed).    ADVANTAGE - The method allows economical production of the solid fuel with excellent calorific value.
NOVELTY - The operating method involves operating SOFC stack (106) to generate fuel exhaust stream and then separating at least one portion of hydrogen from first portion of fuel exhaust stream using hydrogen separator consists of cascaded hydrogen pumps (135) to generate a purified fuel exhaust stream. The purified fuel exhaust stream is recycled to fuel inlet stream, and a portion of fuel inlet stream comprising ammonia is provided to ATO. The air from SOFC stack is provided to the ATO.    USE - Operating method for fuel cell system.    ADVANTAGE - Ammonia is effectively used as fuel source of fuel cell system, and ammonia fuel is made from domestic carbon bearing fuels in process which yield a pure carbon dioxide waste product that is easily sequestered, and ammonia fuel is easily transported by rail, barge, and trucks as a low pressure liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the fuel cell system.    Fuel cell system (100A)    Ammonia fuel source (101)    Air inlet conduit (104)    SOFC stack (106)    Hydrogen pumps (135)
NOVELTY - Gas separation membrane comprises: a porous support (21); and a gas separating active layer (22) disposed on the porous support and comprising a functionalized graphene.    USE - The gas separation membrane is useful in a gas separator for separating: hydrogen and carbon dioxide; hydrogen and carbon monoxide; hydrogen and methane; hydrogen and nitrogen; helium and nitrogen; nitrogen and carbon dioxide; and/or methane and carbon dioxide (all claimed).    ADVANTAGE - The gas separation membrane: has a high gas permeation rate and excellent selectivity for selected gas mixtures; exhibits improved processability and modularity; and can be prepared easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing a gas separation membrane, comprising: providing a composition comprising a functionalized graphene and a solvent; disposing the composition on a porous support to form a coating; and drying the coating to form a gas separating active layer comprising the functionalized graphene on the porous support.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic cross-sectional view of a gas separation membrane.    Porous support (21)    Gas separating active layer (22)
NOVELTY - Improving the transportability of heavy crude oil having viscosity intended to be reduced by an additive, comprises converting natural gas occurring in the vicinity of a crude oil deposit and/or crude oil accompanying gas into a methanol-water mixture.    USE - The method is useful for improving the transportability of heavy crude oil (claimed).    ADVANTAGE - The method improves the transportability of heavy crude oil without any deleterious effect.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for improving the transportability of heavy crude oil.    Air separation plant (8)    Synthesis gas (10)    Compressor (12)    Crude methanol (14)    Further compressor. (16)
NOVELTY - Producing base fertilizer for grapes, involves (a) mixing dry chicken manure, rapeseed straw, bean cake and peanut cake mixture, lees, river mud, fruit residue, dry bagasse and monosodium glutamate, and crushing and adding 1 wt.% organic fertilizer fermenting agent to the mixture and stacking the mixture and fermenting to obtain organic fertilizer, and (b) mixing urea, calcium superphosphate, potassium sulfate, calcium carbonate, magnesium sulfate, borax and ferrous sulfate, and crushing and mixing the mixture with fertilizer to obtain the product.    USE - The method is useful for producing base fertilizer for grape trees (claimed), which is useful for promoting growth, improving drought resistance and quality of fruit, protecting flowers and fruits.    ADVANTAGE - The fertilizer is rich in organic matter, nitrogen, phosphorus, potassium and trace element, improves soil fertility, and slowly release nutrient element to Chinese chestnut tree.    DETAILED DESCRIPTION - Producing base fertilizer for grapes, involves (a) mixing 30-32 wt.% dry chicken manure, 8-10 wt.% rapeseed straw, 4 wt.% bean cake and peanut cake mixture, 6 wt.% lees, 12 wt.% river mud, 4 wt.% fruit residue, 4 wt.% dry bagasse and 5 wt.% monosodium glutamate, and crushing and adding 1 wt.% organic fertilizer fermenting agent to the mixture and stacking the mixture and fermenting to obtain organic fertilizer, and (b) mixing 5 wt.% urea, 12 wt.% calcium superphosphate, 5 wt.% potassium sulfate, 0.6 wt.% calcium carbonate, 0.4 wt.% magnesium sulfate, 0.7 wt.% borax and 0.3 wt.% ferrous sulfate, and crushing and mixing the mixture with fertilizer obtained in step (a) to obtain the product.
NOVELTY - Preparation of lurasidone hydrochloride (I) involves resolving trans(racemic)-1,2-cyclohexane dicarboxylic acid (III) into trans(R,R)-1,2-cyclohexane dicarboxylic acid using chiral amine in presence of co-base, and converting the trans(R,R)-1,2-cyclohexane dicarboxylic acid into the lurasidone hydrochloride.    USE - Preparation of lurasidone hydrochloride used as antipsychotic agent for treatment of schizophrenia.    ADVANTAGE - The method economically and efficiently provides lurasidone hydrochloride with high yield and purity, in a short period of time, with reduced usage amount of solvent and without performing multiple crystallizations. The lurasidone hydrochloride is environmentally-friendly.    DETAILED DESCRIPTION - Preparation of lurasidone hydrochloride of formula (I) involves resolving trans(racemic)-1,2-cyclohexane dicarboxylic acid of formula (III) into trans(R,R)-1,2-cyclohexane dicarboxylic acid using chiral amine in presence of co-base, and converting the trans(R,R)-1,2-cyclohexane dicarboxylic acid into the lurasidone hydrochloride.
NOVELTY - Manufacture of fuel involves producing primary plasma, secondary plasma, tertiary plasma and fueling material plasma, contacting fueling material plasma with tertiary fluid plasma, secondary fluid plasma and primary fluid plasma in processing chamber, forming plasma mixture, cooling plasma mixture using heat exchange (125) device, forming cooled plasma mixture and contacting cooled plasma mixture with catalyst.    USE - Manufacture of fuel e.g. ethanol, methanol, natural gas and digester gas. The fuel comprises naphtha, diesel fuel, diesel fuel blend, JP-8 fuel, jet fuel and jet fuel blend.    ADVANTAGE - The method efficiently enables manufacture of fuel.    DETAILED DESCRIPTION - Manufacture of fuel involves exposing primary working fluid to high-voltage electric field (A), producing primary plasma, exposing secondary working fluid to high-voltage electric field (B), producing secondary plasma, exposing tertiary working fluid to high-voltage electric field (C), producing tertiary plasma, exposing fueling material to high-voltage electric field (D), producing fueling material plasma, contacting fueling material plasma with tertiary fluid plasma, secondary fluid plasma and primary fluid plasma in processing chamber, forming plasma mixture, cooling plasma mixture using heat exchange device, forming cooled plasma mixture and contacting cooled plasma mixture with catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view explaining manufacture of fuel.    High-voltage electric generator (102,105,110)    Primary processing chamber (120)    Heat exchanger (125)    Secondary processing chamber (130)    Fuel storage tank (135)
NOVELTY - Pyrolyzing biomass comprises (a) pyrolyzing a biomass feedstock in a reactor (20), where the pyrolyzing forms products comprising a primary gaseous product and char, and (b) passing the primary gaseous product out of the reactor, where the primary gaseous product passing out of the reactor entrains less of the char as a direct consequence of the biomass feedstock comprising particles that are greater than 300 microns, preferably greater than 750 microns in diameter.    USE - The process is useful for pyrolyzing biomass (claimed) to produce chemical or fuel products including gasoline, jet/kerosene, diesel and gasoil.    ADVANTAGE - The process ensures rapid catalytic upgrading of the primary gaseous products into products, while preventing char and associated metals from entrainment with these vapors to cause catalyst deactivation and equipment fouling and increasing the instability of the product pyrolysis oil.    DESCRIPTION OF DRAWING(S) - The figure shows a pyrolysis reactor with a catalyst vessel to receive and upgrade the vapors from the pyrolysis reactor.    Biomass feedstock inlet (10)    Particulate biomass feedstock (12)    Heat earner inlet (17)    Pyrolysis reactor (20)    Motor. (25)
NOVELTY - Manufacture of combustion-ashes molded product involves adding heavy oil (O) and combustion ashes (A) to biomass (B) and/or waste-plastic crushed product (P), mixing and molding. The mixing rate of the biomass with respect to the total quantity of the molded product raw material and/or the waste-plastic crushed product is 5-30 %mass. The mixing rate of the heavy oil with respect to the total quantity of the molded product raw material is 25-40 %mass.    USE - Manufacture of combustion-ashes molded product used for fuel and reducing agent (all claimed).    ADVANTAGE - The method provides combustion-ashes molded product with favorable strength without drying or heating process. The fuel and reducing agent formed using the combustion-ashes molded product have excellent handling property and safety, and reduced heat loss.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel, which is obtained by molding combustion-ashes molded product into granular form having an average particle diameter of 2-10 mm; and    (2) reducing agent, which is obtained by molding combustion-ashes molded product into granular form having an average particle diameter of 5-20 mm.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram for the manufacture of combustion-ashes molded product. (Drawing includes non-English language text)    Flat die-type molding machine (6)    Combustion ashes (A)    Biomass (B)    Heavy oil (O)    Waste-plastic crushing product (P)
NOVELTY - The water-electrolysis system (10) has a gas-liquid separation apparatus (18) which is provided with a lower water storage portion (44). An upper water storage portion (46u) is connected with the lower water storage portion in gravitational direction. A cross-sectional area of the upper water storage portion is different from the cross-sectional area of the lower water storage portion. A control apparatus (24) is provided with a water-level-control portion (54) to control a drainage apparatus (22), so that a water level is varied within the range of lower water storage portion.    USE - Water-electrolysis system.    ADVANTAGE - Since the control apparatus is provided with water-level-control portion to control drainage apparatus for varying water level within range of lower water storage portion, the detection of electrostatic capacitance type water level can be detected reliably and easily. Thus, the overflow of water from the gas-liquid separation apparatus can be prevented in effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a control method of water-electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of water-electrolysis system. (Drawing includes non-English language text)    Water-electrolysis system (10)    Gas-liquid separation apparatus (18)    Drainage apparatus (22)    Control apparatus (24)    Lower water storage portion (44)    Upper water storage portion (46u)    Water-level-control portion (54)
NOVELTY - Device for drying and torrefaction of biomass, comprises (i) a drying device (24) for drying the biomass to a dried biomass, (ii) a first mixing chamber (25) for a conditioning device for mixing the smoke gas from a steam boiler (21) and/or from a turbine (22) of the plant to a conditioning gas, (iii) the conditioning device for conditioning the dried biomass to a conditioned biomass, and (iv) a second mixing chamber (26) for a torrefaction device for mixing the smoke gas from the steam boiler, the turbine and/or a combustion chamber of the power plant to a torrefied gas.    USE - The device is useful for drying and torrefaction of biomass, preferably by utilizing the waste heat from a power plant.    ADVANTAGE - The device uses the waste heat from the power plant for the torrefaction of biomass, and thus it carries out drying and torrefaction of biomass in an energy and cost efficient manner.    DETAILED DESCRIPTION - Device for drying and torrefaction from biomass, preferably by utilizing the waste heat from a power plant, comprises (i) a drying device (24) for drying the biomass to a dried biomass, (ii) a first mixing chamber (25) for a conditioning device for mixing the smoke gas from a steam boiler (21) and/or from a turbine (22) of the plant to a conditioning gas at a temperature of 200 degrees C, (iii) the conditioning device for conditioning the dried biomass to a conditioned biomass, and (iv) a second mixing chamber (26) for a torrefaction device for mixing the smoke gas from the steam boiler, the turbine and/or a combustion chamber (of the power plant to a torrefied gas at a temperature of 300-400 degrees C. The torrefaction device is provided for torrefaction of the conditioned biomass to a torrefied biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device.    Steam boiler (21)    Turbine (22)    Drying device (24)    First mixing chamber (25)    Second mixing chamber (26)
NOVELTY - Using methanol in an internal combustion engine with self-ignition, comprises heating methanol in a device for internal dehydration, conducting the heated methanol over a catalyst for converting methanol to dimethyl ether, and supplying dimethyl ether together with other reaction products, directly as a combustion fuel to combustion chamber.    USE - The method is useful for using methanol in internal combustion engine with self-ignition (claimed).    ADVANTAGE - The method ensures the usage of methanol which is free of carbon black and has low nitrogen oxide content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for the internal dehydration of methanol in the internal combustion engine with self-ignition, which is arranged on the internal combustion engine or its supply- and discharge pipes which conduct media, comprising a catalyst chamber (K) having a heater, a methanol supply pipe, and a reaction product discharge pipe which is connected with the medium-conducting supply pipe e.g. fuel supply pipe of the internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of flow direction of exhaust gas or fuel.    Exhaust pipe (1)    Double pipe (2)    Exhaust gas stream (A)    Reaction product outlet (B)    Catalyst chamber (K)
NOVELTY - Preparing moxonidine, comprises reacting 4,6-dichloro-2-methyl-5-(1-acetyl-2-imidazolin-2-yl)-aminopyrimidine with an organic base in methanol or in a methanol-containing solvent mixture.    USE - The method is useful for preparing moxonidine (claimed) that is useful as a hypotensive medicament. No biological data given.    ADVANTAGE - The method provides moxonidine with high purity and yield in a safe, economical and eco-friendly manner.
NOVELTY - Selenium-enriched foliar fertilizer is prepared by mixing and stirring raw materials comprising 15 kg water, 0.01 g glutamate, 0.01-15 g lysine, 0.01 g leucine, 0.01 g histidine, 1-50 g methionine, 0.01-35 g cystine, 0.01-15 g threonine, 0.01-15 g phenylalanine, 0.01-40 g serine, 1-40 g tryptophan, 0.01-40 mg vitamin C, 0.01-40 mg vitamin E, 0.01-50 mg vitamin B1, 0.01-40 mg vitamin B6, 0.01-40 mg vitamin B12, 1-60 g potassium hydroxide, and 0.01-2 g coenzyme II.    USE - The selenium-enriched foliar fertilizer is useful for radish cultivation.    ADVANTAGE - The selenium-enriched foliar fertilizer does not contain exogenous selenium, has simple formulation, is easy for preparation, promotes growth, color, anthocyanin content and virus and stress resistance of radish, has selenium content of 0.01 mg/kg, reduces agricultural production cost and environmental pollution, and provides improved economic benefit and ecological benefit.
NOVELTY - Method for recovering scandium involves providing aqueous solution (12) containing dissolved EDTA salts, contacting (14) solution with a scandium-containing material (10) such that scandium and other impurity metal(s) are transferred into the solution to produce a scandium loaded solution, separating depleted scandium-containing material from scandium loaded solution, treating scandium loaded solution by increasing pH to precipitate impurity metal(s) and avoiding precipitation of scandium, and further increasing pH of aqueous solution to precipitate scandium.    USE - Method for recovering scandium used as alloying agent in aluminum alloy for manufacture of aircraft, baseball bat, bicycle frame and bicycle component, and for fuel cell and manufacture of high intensity discharge lamp.    ADVANTAGE - The method enables recovery of high purity scandium with selective removal of iron, aluminum, titanium, chromium, silicon, and zirconium from the scandium loaded solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of method for recovering scandium.    Scandium-containing material (10)    Aqueous solution (12)    Contacting process (14)    Sulfide material (26)    Caustic soda solution (32)    Solid scandium-containing product (42)
NOVELTY - A resveratrol is enzymatically converted by inoculating Alternaria (CCTCC M2011348) into liquid culture medium at 28 degrees C under 120 rpm for 4 days, filtering, collecting mycelium, washing by distilled water, grinding in liquid nitrogen, adding 4 g mycelium every 8 ml crude enzyme extracting solution, adding enzyme extracting solution, mixing uniformly, centrifuging at 4 degrees C under 1000 rpm for 10 minutes, collecting supernatant, adding solid ammonium sulfate in 75% concentrated supernatant, standing overnight, centrifuging at 4 degrees C under 1000 rpm for 10 minutes, and collecting precipitate.    USE - Enzymatic conversion of resveratrol (claimed).    ADVANTAGE - Enzymatic conversion process is safe, environment-friendly, and low in cost, and has high production efficiency and strong controllability.    DETAILED DESCRIPTION - A resveratrol is enzymatically converted by inoculating Alternaria (CCTCC M2011348) into liquid culture medium at 28 degrees C under 120 rpm for 4 days, filtering, collecting mycelium, washing by distilled water, grinding in liquid nitrogen, adding 4 g mycelium every 8 ml crude enzyme extracting solution, adding enzyme extracting solution, mixing uniformly, centrifuging at 4 degrees C under 1000 rpm for 10 minutes, collecting supernatant, adding solid ammonium sulfate in 75% concentrated supernatant, standing overnight, centrifuging at 4 degrees C under 1000 rpm for 10 minutes, collecting precipitate, drying, putting crude enzyme extracting solution into dialysis bag, dialyzing at 4 degrees C until no sulfate ion (SO4)2-, detecting dialysis liquid to obtain crude enzyme solution, taking 100 ml buffer solution, adding 5-50 ml crude enzyme solution, and reacting at 37 degrees C under 120 rpm for 0.5-4 hours.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of resveratrol reaction system in different pH conditions. (Drawing includes non-English language text).
NOVELTY - A tonifying spleen and helping digestion pineapple sago contains 80-100 pts. wt. sago, 30-40 pts. wt. pineapple, 20-30 pts. wt. mulberry, 30-40 pts. wt. yellow peach, 35-45 pts. wt. yam, 20-30 pts. wt. pear, 5-10 pts. wt. lotus seed, 3-5 pts. wt. Chinese wax gourd peel, 3-5 pts. wt. arbuscular mycorrhizal, 5-6 pts. wt. hawthorn, 5-7 pts. wt. dried orange peel, 4-5 pts. wt. tuckahoe, 5-6 pts. wt. Radix codonopsitis, 2-3 pts. wt. camphor leaf, 2-3 pts. wt. medlar leaf, 50-60 pts. wt. honey, 20-30 pts. wt. rice wine, and water.    USE - A tonifying spleen and helping digestion pineapple sago for patient with dyspepsia.    ADVANTAGE - Preparation process is simple and environment-friendly, and product is refreshing and has tonified spleen, good digestion effect, and sweet taste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of tonifying spleen and helping digestion pineapple sago which involves cleaning pineapple, peeling, cutting into blocks, pouring sago into pot, adding 2-3 times water, heating, stirring constantly, boiling pineapple with lotus seed, heating continuously, stirring, peeling mulberry, yellow peach, yam, and pear, removing seed, cutting into blocks, heating rice wine for 30-40 minutes, cooling, marinating for 1-2 days, heating Chinese wax gourd peel, arbuscular mycorrhizal, hawthorn, dried orange peel, tuckahoe, R. codonopsitis, camphor leaf, and medlar leaf with 3-5 times water to extract, condensing, mixing Chinese medicine concentrated solution and honey, pouring into sago, mixing uniformly, cooling, and pouring mulberry, yellow peach, yam, and pear into sago.
NOVELTY - Method for preparing liquid fertilizer using effective microrganism (EM) and fermented Cordyceps residue conversion, involves processing the fermented residual liquid, filtering, fermenting C.sinensis to obtain proliferation liquid, using EM bacteria, separating the photosynthetic bacteria, lactic acid bacteria, microzyme, and filamentous bacteria to prepare EM active solution, adding proliferation liquid to fermentation tank, adding EM active liquid and uniformly mixing and sealing product.    USE - The method is useful for preparing liquid fertilizer using EM and fermented Cordyceps residue conversion which is used in planting different types of crops, preferably grain crops, cash crop or fruit and vegetable (all claimed).    DETAILED DESCRIPTION - Method for preparing liquid fertilizer using effective microrganism (EM) fermented Cordyceps residue conversion, involves processing the fermented residual liquid, filtering, fermenting C.sinensis to obtain proliferation liquid, using EM bacteria chosen from photosynthetic bacteria, lactic acid bacteria, microzyme, and filamentous bacteria, separating the photosynthetic bacteria, lactic acid bacteria, microzyme, Actinomyces bacteria and filamentous bacteria to prepare EM active solution, adding proliferation liquid to fermentation tank, adding EM active liquid and uniformly mixing and sealing product.
NOVELTY - Producing compound fertilizer, involves (a) adding rice husk powder and cake flour powder into water, mixing uniformly and covering the mixture using plastic film, and fermenting for several days at high temperature continuously and gradually decreasing the temperature to attain maturity, and (b) mixing effective microorganism, photosynthetic bacteria, fermented material and sodium humate and packing the product.    USE - The method is useful for producing compound fertilizer (claimed).    ADVANTAGE - The method enables to increase beneficial bacteria number, thus is increases the yield.    DETAILED DESCRIPTION - Producing compound fertilizer, involves (a) adding 1000 kg rice husk powder and 20 kg cake flour powder into 700 kg water, mixing uniformly and covering the mixture using plastic film, and fermenting the mixture by raising the temperature of the stack to 50 degrees C after 24 hours of stacking and raising the temperature to 70 degrees C after 48 hours of stacking, and fermenting for several days at high temperature continuously and gradually decreasing the temperature for 10-15 days to attain maturity, until all microorganism are killed, where the fermented material will be brown or dark brown and soft, and (b) mixing effective microorganism, photosynthetic bacteria, fermented material and sodium humate in ratio of 1:1;10:1 and packing the product, where the cake flour powder is one, two or more chosen from peanut Cake powder, bean cake powder and cottonseed cake powder.
NOVELTY - Fertilizer comprises polyacrylamide, epsilon -polylysine, matrine, calcium propionate, ascorbic acid, EDTA, potassium fulvate, zinc chloride and composite microbial inoculum.    USE - The fertilizer is useful for apple tree (claimed) for preventing apple oxidation, inhibiting harmful microbial growth and preventing browning of apple on its surface.    ADVANTAGE - The fertilizer has stable structure and function, causes no toxic side effects, can replace the chemical fertilizer in the agricultural production, can form a protective layer, and improves quality and yield of product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves obtaining the composite microbial inoculum by obtaining fermentation liquid of each strain after performing fermentation and mixing obtained liquids, adding the above-mentioned remaining raw materials, uniformly stirring, adding water to dilute and obtaining product.
NOVELTY - Mushroom culture base material comprises raw materials comprising 85 wt.% agricultural waste, 12 wt.% wheat bran or rice bran, 1.5 wt.% lime powder, 1 wt.% gypsum powder and 0.5 wt.% urea, where the mass ratio of dry substance is 100%.    USE - As mushroom culture base material.    ADVANTAGE - The culture base material enables to increase growth of mushroom, has anti-impurity capability and harmful substance residue, effect of more than 99%, shortens production period, improves production and quality of mushroom, and provides yield of more than 20%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the culture base material, which involves drying the raw materials for 1-2 days, killing bacteria in raw material by UV ray before mixing, uniformly agricultural waste, lime powder and urea in dry state, fermenting mixture, piling wet material at a height of 1-1.2 m, controlling dry weight of culturing material to 250-500 kg, finally covering tarpaulin, fermenting, turning when the material temperature reaches 60 degrees C, maintaining mixture for 24 hours, taking every day, turning one time, adding wheat bran or rice bran and gypsum powder, further adding salt and water, turning for 3-4 times, and fermenting mixture for 5-6 days until the water content is 63-65%.
NOVELTY - A biological organic fertilizer comprises 20-25 pts. wt. cow dung, 10-15 pts. wt. cattle manure, 10-15 pts. wt. sheep manure, 12-15 pts. wt. peat soil, 6-10 pts. wt. animal bone, 4-6 pts. wt. animal stucco, 4-6 tree leaves, 6-8 pts. wt. mushroom residue, 0.01-0.03 pts. wt. copper oxide, 0.01-0.03 pts. wt. ferric oxide, 0.01-0.03 pts. wt. magnesium, 2-4 pts. wt. humic acid, 0.01-0.03 pts. wt. potassium, 2-4 pts. wt. straw, 1-3 pts. wt. egg shell powder, 1-2 pts. wt. rice bran, 0.5-0.8 pts. wt. glucose and 0.05-0.08 pts. wt. borax.    USE - Biological organic fertilizer (claimed).    ADVANTAGE - The biological organic fertilizer has large fertility, and protects ecological balance.    DETAILED DESCRIPTION - A biological organic fertilizer comprises 20-25 pts. wt. cow dung, 10-15 pts. wt. cattle manure, 10-15 pts. wt. sheep manure, 12-15 pts. wt. peat soil, 6-10 pts. wt. animal bone, 4-6 pts. wt. animal stucco, 4-6 tree leaves, 6-8 pts. wt. mushroom residue, 0.01-0.03 pts. wt. copper oxide, 0.01-0.03 pts. wt. ferric oxide, 0.01-0.03 pts. wt. magnesium, 2-4 pts. wt. humic acid, 0.01-0.03 pts. wt. potassium, 0.03-0.06 pts. wt. Azotobacter, 0.01-0.03 pts. wt. phosphobacteria, 0.01-0.03 pts. wt. potassium bacteria, 2-4 pts. wt. straw, 1-3 pts. wt. egg shell powder, 1-2 pts. wt. rice bran, 0.5-0.8 pts. wt. glucose and 0.05-0.08 pts. wt. borax. An INDEPENDENT CLAIM is included for preparation of organic biofertilizer, which involves stirring raw materials, mixing uniformly, obtaining mixed material, composting mixed material at high temperature for 6-8 days, controlling the temperature at 55-65 degrees C, cooling after high temperature compost processing, adding 0.3 g/ton rice vinegar with respect to 1000 g/ton disinfecting liquid, sterilizing, sealing, and fermenting for 4-7 days.
NOVELTY - Hydrogen syngas production of methane comprises converting synthesis gas into hydrogen-rich purge gas, methanol vapor raw material into purified gas mixture and methanol vapor into mixed gas; feeding mixed gas into first reactor for first reaction with catalyst; feeding first reaction gas and remaining gas mixture into second reactor for second reaction with catalyst; feeding second reaction gas into third section reactor for third reaction; performing third reaction gas-liquid separation; and collecting released product gas.    USE - Hydrogen syngas production of methane.    ADVANTAGE - The method uses methanol instead of carbon, uses hydrogen-rich gas for synthesis gas generation, and further consumes residual hydrogen thus overcoming problems of consuming carbon hydrogen resources.    DETAILED DESCRIPTION - Hydrogen syngas production of methane comprises converting synthesis gas into hydrogen-rich purge gas, methanol vapor raw material into purified gas mixture and methanol vapor into mixed gas, in which methanol vapor is 20-50 vol.% of mixture; feeding mixed gas into first reactor for first reaction with catalyst; feeding first reaction gas and remaining gas mixture into second reactor for second reaction with catalyst; feeding second reaction gas into third section reactor for third reaction; performing third reaction gas-liquid separation; collecting released product gas; and discharging methanol and water from system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a process for hydrogen syngas production of methane (Drawing includes non-English language text).
NOVELTY - Recovery of remixed alcohol comprises extracting and rectifying non-acid oxygenated organic compound to obtain mixed alcohol containing heavy mix alcohol with an aqueous solution containing extractant, carrying out Fischer-Tropsch synthesis with water, deacidifying, and distilling; mixing aqueous solution containing alcohol, adding extractant, distilling, and recovering extractant; mixing and layering, where upper layer is organic phase; and mixing organic phase with remixed alcohol, distilling, and separating remixed alcohol.    USE - Method for recovering remixed alcohol (claimed) used as fuel.    ADVANTAGE - The method adopts multiple rectifying operation unit. The product has high purity and high heat value and greatly increases solid fuel liquefied-making device.
NOVELTY - A 1,3-acetoin is purified by decompressing and distilling fermentation liquid under reduced pressure at 60-90 degrees C, centrifuging, recycling condensed liquid, determining using gas chromatography, osmotic distilling using polyethylene hollow fiber membrane or polyvinylidene difluoride membrane with 45-55 wt.% calcium chloride or 15-20 wt.% sodium chloride as extracting medium at 45-55 degrees C and feed rate of 55-70 L/hour, and controlling concentration of calcium chloride and sodium chloride.    USE - Method for purifying 3-butanone.    ADVANTAGE - The method is simple, environment-friendly, has mild reaction condition, high purity and easy-to-scale extraction.
NOVELTY - A L(+)-2,3-dihydroxysuccinic acid is prepared by reacting L-methyldopa, inorganic calcium salts and L(+)-2,3-dihydroxy-sodium succinate (III) to obtain L(+)-2,3-dihydroxy-calcium succinate (II), centrifuging to obtain L(+)-2,3-dihydroxysuccinic acid calcium (II), suspending with water and aqueous sulfuric acid, generating L(+)-2,3-dihydroxysuccinic acid (I) and inorganic calcium salt, filtering to obtain L(+)-2,3-dihydroxysuccinic acid (I), activated carbon decoloring, hot filtering, concentrating under reduced pressure, crystallizing, centrifuging to obtain crude product and crystallizing.    USE - Method for preparing L(+)-2,3-dihydroxysuccinic acid (claimed).    ADVANTAGE - The method is simple, environment-friendly, has mild reaction condition and easy to control, high product purity and yield, stable technique and reduces production cost.    DETAILED DESCRIPTION - A L(+)-2,3-dihydroxysuccinic acid is prepared by reacting L-methyldopa, inorganic calcium salts and 5-10 wt.% L(+)-2,3-dihydroxy-sodium succinate (III) at 60 degrees C for 10-60 minutes to obtain L(+)-2,3-dihydroxy-calcium succinate (II) precipitate, centrifuging, to obtain L(+)-2,3-dihydroxysuccinic acid calcium (II), suspending with water and 20-40 wt.% aqueous sulfuric acid, generating L(+)-2,3-dihydroxysuccinic acid (I) and inorganic calcium salt, filtering to remove inorganic calcium salt to obtain L(+)-2,3-dihydroxysuccinic acid (I) aqueous solution, activated carbon decoloring at 30-100 degrees C for 10-60 minutes, hot filtering, concentrating under reduced pressure, crystallizing at -5-10 degrees C for 30-60 minutes, centrifuging to obtain crude product, recrystallizing with purified water at 60-10 degrees C for 20-40 minutes, dissolving, hot filtering, crystallizing at -5-10 degrees C for 30-60 minutes, centrifuging and drying at 50-100 degrees C for 4-6 hours.
NOVELTY - Erythromycin A streptomyces fermentation medium has primary seed culture, secondary seed culture medium and fermentation culture medium. The primary seed culture, secondary seed culture medium and fermentation culture medium contain sucrose and corn steep liquor.    USE - Erythromycin A streptomyces fermentation medium is used for preparing erythromycin (claimed).    ADVANTAGE - The erythromycin A streptomyces fermentation medium has reduced viscosity and residual solids at the end of fermentation, and reduces the amount of slag and bacteria in wastewater without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermentation process for production of erythromycin, which involves sterilizing spores of streptomyces erythromycin by adding primary seed culture at culture temperature of 32-36 degrees C, stirring for 45-60 hours, inoculating, adding secondary seed cultivation liquid at culture temperature of 32-36 degrees C, adding fermentation culture medium, and stirring for 160-180 hours.
NOVELTY - Organic cultivating substrate comprises raw materials comprising 20-27 pts. wt. vinegar, 15-20 pts. wt. Chrysanthemum stalk, 10-15 pts. wt. canal mud, 7-12 pts. wt. plant ash, 5-10 pts. wt. bean cake, 5-10 pts. wt. double-bottom rape vegetable cake, 5-12 pts. wt. potassium sulfate, 7-10 pts. wt. calcium magnesium phosphate and 1-5 pts. wt. amino acid.    USE - The organic cultivating substrate is useful for preventing epidemic disease and gray mold of leek.    ADVANTAGE - The substrate can be produced simply as raw materials are easily available, provides good appearance of product, utilizes agricultural waste, is convenient to use and environmentally-friendly, and reduces loss of nitrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic cultivating substrate, which involves (a) adding water to the bean cake, rape vegetable cake, canal mud and amino acid, covering and sealing the raw material using plastic thin film for 7-12 days after fermentation to obtain ecological amino acid fermenting material, (b) drying Chrysanthemum straw, mechanically crushing, adding potassium sulfate and calcium magnesium phosphate fertilizer, pulverizing the mixture to 20-60 meshes, adding vinegar residue and plant ash into fermentation tank, performing high temperature anaerobic fermentation at 60-70 degrees C for 10-20 days to remove fermentation raw material, and (c) mixing ecological amino acid fermenting material and microorganism substrate fertilizer with mixer to obtain mixed material, drying at low temperature, crushing to 60-100 meshes, and packaging obtained product.
NOVELTY - The system has a groove that is formed on needed area of a bed surface (3) of the compost material (9). A compost material collector is set to collect the microorganism and water of the desired amount from compost material. An output hole of the compost raw material is formed in microwave propagation tube (15) arranged in microwave oscillation device (19). The compost material is set to absorb moisture contained in output of heat compost raw material.    USE - System for manufacturing heat compost raw material.    ADVANTAGE - The high efficiency heating compost materials can be obtained by heating the compost material in water so as to create a good environment for microbial activity. The power consumption and manufacturing cost of system for manufacturing heat compost raw materials can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing heat compost raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating the process for manufacturing heat compost raw materials.    Bed surface of the compost material (3)    Compost material (9)    Air delivery tube (11)    Microwave propagation tube (15)    Microwave oscillation device (19)
NOVELTY - The system has a gasifier (116) for gasifying a gasification raw material using a catalyst and generating gasifying gas. A cleaning purification part cleans and purifies generated gasifying gas using water and generates the purified-gas-ized gas. A precipitating part (330) precipitates a catalyst derived substance i.e. calcium oxide, contained in waste water, which arose in the cleaning purification part to provide acidic gas contact. A return part (320) returns the catalyst derived substance to the gasifier. An isolation part (222) isolates acidic gas from the purified-gas-ized gas.    USE - System for generating gasifying gas by gasifying gasification raw materials such as coal, biomass and tire chip. Uses include but are not limited to an electric power generation system, a hydrogen manufacturing system, a manufacturing system of synthetic fuel i.e. synthetic petroleum and a manufacturing system of chemical fertilizer i.e. urea.    ADVANTAGE - The precipitating part precipitates the catalyst derived substance contained in the waste water, which arose in the cleaning purification part to provide acidic gas contact so as to remove catalyst derived substance from the waste water in a better manner. The system is simple in structure and inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gasifying gas generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a combination structure of a gasification gas purification apparatus and a waste water treatment equipment.'(Drawing includes non-English language text)'    Gasifier (116)    Isolation part (222)    Return part (320)    Precipitating part (330)    Waste-water-treatment part (360)
NOVELTY - Method for reducing molecular weight of organic substance involves adding excess steam to waste gas containing carbon monoxide produced in metallurgical furnace, performing shift reaction, obtaining mixed gas containing hydrogen and carbon dioxide gas produced by shift reaction and steam which is not consumed by shift reaction, contacting the obtained mixed gas with an organic substance in fluidized-bed (4) in which flow medium is a granular material having true density of 4-8 g/cm3 and containing chromium, iron or nickel, modifying, and rendering low molecular weight.    USE - Method for reducing molecular weight of organic substance e.g. plastics, oil-impregnated sludge, waste oil, biomass and molding mixture of plastic and timber e.g. construction scrap wood, packing/transportation scrap wood, and coppiced timber and producing gas product used as reduction material and fuel for operating blast furnace (all claimed).    ADVANTAGE - The method efficiently reduces the molecular weight of organic substance without producing plastic melt within a reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for operating blast furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of modifier for rendering organic substance low molecular weight. (Drawing includes non-English language text)    Fluidized-bed reactor (1)    Discharge pipe (2)    Fluidized-bed (4)    Return pipe (5)    Dispersing plate (10)
NOVELTY - A biological organic fertilizer comprises 45-50 wt.%, preferably 50 wt.% chicken manure, 20-25 wt.%, preferably 20 wt.% vinasse powder, 10-12 wt.%, preferably 10 wt.% rapeseed, 8-10 wt.%, preferably 8 wt.% Phellodendron, 5-8 wt.%, preferably 8 wt.% phosphate fertilizer, 1 wt.% fermenting agent and 3 wt.% sulfuric acid.    USE - The fertilizer meets NY525-2012 which is a standard for biological organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biological organic fertilizer comprising mixing raw materials and water, reacting at more than 100 degrees C, fermenting at 50-65 degrees C for 10 days, crushing and sieving, checking and packaging.
NOVELTY - Degrading gallic acid in wastewater by Aspergillus oryzae, comprises taking Aspergillus oryzae as a parental strain and carrying out test tube expansion culture, shake-flask liquid culture and strain liquid expanding culture, harvesting by centrifugation and removing gallic acid in wastewater using strain cells.    USE - The method is useful for degrading gallic acid in wastewater by Aspergillus oryzae.    ADVANTAGE - The method achieves gallic acid removal rate of 60-100% (claimed).
NOVELTY - A cultivation nutrient material comprises 84-89 wt.% vinegar, 10-15 wt.% bran and 1 wt.% calcium carbonate.    USE - Cultivation nutrient material used for edible mushroom.    ADVANTAGE - The nutrient material is low cost.    DETAILED DESCRIPTION - An INDPENDENT CLAIM is included for preparation of cultivation nutrient material comprising concentrating vinegar, adding bran and calcium carbonate, mixing, sterilizing at 100 degrees C for 10-12 hours, adjusting to 7-8 pH, fermenting at 65 degrees C for 8-10 days, cooling to room temperature, and sterilizing at 100 degrees C for 10-12 hours.
NOVELTY - Fertilizer formulation comprises 35-40 pts. wt. organic material, 15-20 pts. wt. nitrogenous fertilizer, 10-15 pts. wt. phosphate fertilizers, 15-22 pts. wt. potash fertilizers, 31 pts. wt. trace element, and 5-10 pts. wt. mineral conditioning agent.    USE - Fertilizer formulation used for Stevia rebaudiana (claimed).    ADVANTAGE - The formulation promotes crop growth, yield and quality of Stevia rebaudiana. The method is environment-friendly, reduces production cost and improves efficiency.
NOVELTY - Linear polystyrene supported (S)-5-(4-methoxybenzyl)-3-phenyl-1-propionyl hydantoin derivative (I) is new. The molecular weight of (I)is 8400-14000.    USE - (I) is used as chiral auxiliary reagent for inducing asymmetric aldol condensation (claimed). Chiral compound with high optical purity is used as medicine, pesticide, spice, functional material precursor, and intermediates.    ADVANTAGE - (I) as chiral auxiliary reagent can induce homogeneous and quick asymmetric reaction, and assures convenient detection, and maintains chiral based hydantoin to induce high yield and high stereo-selectivity, and produces chiral compound with high optical purity; and is easy to recycle.    DETAILED DESCRIPTION - Linear polystyrene supported (S)-5-(4-methoxybenzyl)-3-phenyl-1-propionyl hydantoin derivative of formula (I) is new. The molecular weight of (I)is 8400-14000.    m:n = 1:1-4.    An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - The utility model claims one new type generator of air with amino acid chelate and humic acid organic-inorganic compound fertilizer production device, belonging to the fertilizer field, comprising a concentrating tank, a filter, a chemical reaction kettle, a crusher, a fermenting tank, a mixing machine, a granulator, drier, wherein the concentrating tank and filter is provided with a first slurry pump and pipeline between the filter and the chemical reaction kettle is provided with a second slurry pump and pipeline, the chemical reaction kettle and mixing machine is provided with a third slurry pump and pipeline, between the crusher and the fermentation tank is provided with a first conveyor, a crusher and mixing machine is provided with a second conveyor, mixing machine and granulator is provided with the third conveyor, and the dryer is provided with conveyor, wherein the whole slurry pump is a stainless steel slurry pump, pipe is polyethylene pipe, said first conveyor's is a bidirectional scraper conveyor The second, the third and the fourth conveyor is a one-way scraper type conveying machine.
NOVELTY - Straw-degrading fungus Penicillium oxalicum (JSD-17) strain (CGMCC NO.7743), is new.    USE - For treating fungal degradation of agricultural waste straw compost fermentation; and for preparing fertilizer (claimed).    ADVANTAGE - The rice-degrading fungus Penicillium oxalicum (JSD-17) strain not only has a strong cellulose synthetic capability, but also has a straw decomposition of hemicellulose and pectin components; and is synthesized laccase (Lac), lignin peroxidase enzymes (Lip) and manganese peroxidase (Mnp).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer involving inoculating the Penicillium oxalicum (JSD-17) strain into culture medium, where the culture medium comprises 200 g of peeling potato, 20 g of glucose, 15 g of agar, and 1000 ml of anti-steaming water; fermenting at 32 degrees C for 72 hours, collecting bacteria liquid, and conducting culture box incubation at 30 degrees C for 24 hours.
NOVELTY - Cellulose degrading bacteria JSD-12, selected from Bacillus pumilus with preserving number of CGMCC N0.7923 is new.    USE - For preparation of straw biological organic fertilizer (claimed).    ADVANTAGE - The cellulose degrading bacteria JSD-12 is biological environment-friendly with phosphorus's ability; has strong degradation ability to the cellulose, has pair of semi-cellulose and pectin in the straw with a certain component's decomposition ability; quickly and can bear high temperature more than 60 degrees C, it can be made into microbial inoculum adding's high temperature composting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of straw biological organic fertilizer involving: using cellulose degrading bacteria with high temperature pile fertilizer agent so as to prepare rice straw biological organic fertilizer; or asparagus straw crushing device to crush into 5-10 cm, forming straw section in, according to straw weight's 0.5-1.0% access compost microbial inoculum, regulating water content of stack at 65%; measuring stack temperature every day, to stack temperature rapidly to 70 degrees C, and maintaining for 1-2 days, when the temperature does not rise and gradually reduced to less than 45 degrees C, finishing the first fermentation, and then taking, namely 7-8 days turning 1-time, turning for 3 times, after the third time is finished, to obtain the straw biological organic fertilizer.
NOVELTY - Method for improving yield of paclitaxel from Taxus chinensis, involves using T.chinensis buds as explants, removing the outer small portions, adding 0.5-2 mg/l 2,4-dichlorophenoxyacetic acid (2,4-D) and/or 0.5-3 mg/l 1-naphthaleneacetic acid (NAA) in modified Murashige and Skoog (MS) culture medium, culturing at 23-25 degrees C under dark for 35-40 days, selecting light green or white callus, transferring above-mentioned components and 0.2-1 mg/l kinetin in Gamborg medium (B5), culturing, and collecting the callus can be collected for extracting product.    USE - The method is useful for improving yield of paclitaxel from T.chinensis (claimed).    ADVANTAGE - The method exhibits improved yield up to 62.5%, and low browning which enables accumulation of paclitaxal, and is environmentally-friendly.    DETAILED DESCRIPTION - Method for improving yield of paclitaxel from Taxus chinensis, involves using T.chinensis buds as explants, removing the outer small portions, adding 0.5-2 mg/l 2,4-dichlorophenoxyacetic acid (2,4-D) and/or 0.5-3 mg/l 1-naphthaleneacetic acid (NAA) in modified Murashige and Skoog (MS) culture medium, culturing at 23-25 degrees C under dark for 35-40 days, selecting light green or white callus, transferring above-mentioned 2,4-D and NAA and 0.2-1 mg/l kinetin (KT) in Gamborg medium (B5), culturing at 23-25 degrees C under dark for 35-40 days, and collecting the callus can be collected for extracting product.
NOVELTY - A pyridine-containing 1,3,4-oxadiazole derivative is synthesized by reacting 2-naphthalen-5-(4-(bromomethyl) phenyl)-1,3,4-oxadiazole, and triethyl phosphite, refluxing, removing excess triethyl phosphite, stirring, adding hexane to precipitate, and tetrahydrofuran to obtain product A, adding 2-pyridine aldehyde, or 4-pyridine aldehyde, dissolving in N,N-dimethylformamide, adding 15-30 mass% potassium tert-butoxide, and anhydrous ethanol, reacting by Wittig-Horner reaction, cooling, filtering, washing at volume ratio of 2-3, mixing dimethyl sulfoxide and ethanol solution, and reacting.    USE - Synthesis of pyridine-containing 1,3,4-oxadiazole derivative for pesticides (claimed).    ADVANTAGE - The derivative has insecticidal activity, and method is environment-friendly, highly efficient, and has important application value.    DETAILED DESCRIPTION - A pyridine-containing 1,3,4-oxadiazole derivative of formula (I) is synthesized by reacting 2-naphthalen-5-(4-(bromomethyl) phenyl)-1,3,4-oxadiazole, and oily triethyl phosphite, mixing, dissolving, refluxing at 125-130 degrees C for 3-5 hours, removing excess triethyl phosphite, stirring, adding hot hexane to precipitate, and tetrahydrofuran to obtain product A, adding equal amounts of product A and 2-pyridine aldehyde, or 4-pyridine aldehyde, dissolving in N,N-dimethylformamide to obtain solution, adding 15-30 mass% potassium tert-butoxide, and anhydrous ethanol, reacting by Wittig-Horner reaction, cooling, filtering, washing at volume ratio of 2-3, mixing dimethyl sulfoxide and ethanol solution, and reacting.    R=2-pyridine, or 4-pyridine.    DESCRIPTION OF DRAWING(S) - The drawing shows a UV absorption spectrum of pyridine-containing 1,3,4-oxadiazole derivative. (Drawing includes non-English language text).
NOVELTY - Method for preparing fertilizer using leachate of livestock manure involves sterilizing and chemical treating the livestock manure using strongly acidic or alkaline chemicals at pH of 10, extracting leachate of the sterilized manure in buried storage tank, preparing slurry by mixing the extracted leachate and bottom ash leachate at constant rate, heat-treating the prepared slurry, and mixing with fermented microorganism, and performing microbial fermentation.    USE - The method is useful for preparing fertilizer using leachate of livestock manure (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer which is prepared by the above-mentioned method.
NOVELTY - The structure has air supply pipe (45) with supply hole for supplying air to multiple blades within reaction tank (10). A blower is arranged in inner side of reaction tank, such that air of blade is fed to mixing unit by compressor connected to air aeration pipe for air-supply within the reaction tank bottom surface. A guide plate (70) is formed in space corresponding to front of supply hole, such that supply hole is blocked.    USE - Air supply structure of treating apparatus of organic waste such as rice hulls, saw dust and waste from livestock shed and poultry or chick farm.    ADVANTAGE - The temperature of reaction tank is maintained, so that high-quality organic material compost can be obtained. The fermentation capacity is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the guide plate connected inside reaction tank.    Reaction tank (10)    Air supply pipe (45)    Guide plate (70)
NOVELTY - Process (P1) for preparation of ethanesulfonyl chloride derivatives involves: treatment of corresponding hydroxyl sulfonic acid derivatives with chlorinating agents and recovering side products.    USE - For preparation of ethanesulfonyl chloride derivatives, such as 2-chloroethanesulfonyl chloride (all claimed), which is useful as intermediate for N-methyl-3-(1-methyl-4-piperidinyl)-1H-indole-5-ethanesulfonamide (Naratriptan) that is drug used for treatment of migraine headaches.    ADVANTAGE - The process allows for preparation of ethanesulfonyl chloride derivatives, particularly 2-Chloroethanesulfonyl chloride; is environmental friendly i.e. green process, and overcomes problem of generation of large quantities of liquid waste resulting from conventional processes, where all the steps in process are environment friendly. The process overcomes problem of generation of large quantities of gaseous waste resulting from conventional processes, recovers one of major and most polluting side products i.e. phosphorus oxychloride, by generating dilute aqueous phosphoric acid during isolation of product, where after isolation of product 9 wt./vol.% aqueous diluted phosphoric acid is formed, aqueous stream generated contains only phosphoric acid and quenching of reaction mass is done after recovery of phosphorus oxychloride, achieves almost complete conversion, can be easily scaled up to commercial level, and is economical commercial process. The dilute phosphoric acid generated can be used for variety of applications, such as can be converted into commercially useful products e.g. disodium phosphate and trisodium phosphate; ammonium phosphate which can be used for agricultural purposes; and tricalcium phosphate which is major component of rock phosphate, naturally occurring raw material for phosphoric acid production.
NOVELTY - Tissue culture method of Dendrobium, involves (a) sterilizing explant using 75 vol.% alcohol for 30-60 seconds, 15-20 vol.% sodium hypochlorite and sterile water, (b) cutting leaves using scalpel, incubating the leaves under dark conditions, and transferring the incubated the explant to light, (c) inducing adventitious buds, (d) cutting shoots into single buds, and inoculating in rooting medium, and (e) carrying out hardening.    USE - Tissue culture method of Dendrobium (claimed).    ADVANTAGE - The method is cost-effective, environmentally-friendly rapid and simple. The cultured Dendrobium is of excellent quality.
NOVELTY - Method for breeding earthworms, involves smashing mushroom culture waste, adding the smashed culture waste in 20% land, and mixing earthworm in the culture waste.    USE - The method is useful for breeding earthworms.    ADVANTAGE - The method is performed in low temperature and rapid, improves nutrition in the culture medium, simply digests and absorbs mushroom, and recycles mushroom culture waste.
NOVELTY - Preparing angiotensin (I) comprises (a) preparing protected angiotensin (II), and (b) deprotecting of (II) in presence of cleaving reagent and separating resin.    USE - (I) is useful for preparing angiotensin peptide drugs (claimed).    ADVANTAGE - The method: is environmentally-friendly; utilizes less equipment; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Preparing angiotensin of formula (H-asparagine-arginine-valine-tyroisne-valine-histidine-proline-phenylalanine-OH) (I) comprises (a) preparing protected angiotensin of formula (R1-asparagine-arginine(R2)-valine-tyroisne(R3)-valine-histidine(R4)-proline-phenylalanine-(R5)) (II), and (b) deprotecting of (II) in presence of cleaving reagent and separating resin.    R1 = amino protecting group (tert-butyloxycarbonyl);    R2 = side chain protecting group (2,2,4,6,7-pentamethyldihydrobenzofuran-5-sulfonyl);    R3 = side chain protecting group (tert-butyl);    R4 = side chain protecting group (trityl); and    R5 = carboxy resin (para hydroxybenzyl alcohol on polystyrene).    An INDEPENDENT CLAIM is also included for angiotensin (I) prepared by above method.
NOVELTY - This utility model claims a kind of marsh gas preparation device, comprising a biogas tank, further comprising acidifying tank, the acidification tank is provided with a feeding port and a discharging port, a discharging port and the feed port of the marsh gas pool of the acidification tank through a valve, the acidifying pool is not less than the inner bottom surface of the marsh gas tank. This utility model has simple structure, low manufacturing cost, quick speed, high, convenient use, safety and reliability.
NOVELTY - This utility model claims a kind of artificial wetland denitrifying sewage treatment system and a continuous sand filtering denitrification device, wherein the artificial wetland denitrifying sewage processing system, comprising a marsh tank, wherein the marsh tank are installed with continuous sand filtering denitrification device, the denitrification filter device comprises a filter, a filter, a filter, a water inlet pipe and a water outlet pipe, a water inlet pipe connected with the inner filter unit, the filter and internal filtering unit and then through a water outlet pipe, the internal filtering unit comprises a water distributor, a central sand extracting pipe, a washing machine and a washing water outlet pipe, the lower end of the middle part of the centre extracting sand pipe of the centre extracting sand pipe is located on the filter bed to extend to the upper end of the central pipe of the extracting sand filter bed extends to the upper part of the filter bed, washing machine is set on the upper end of the centre extracting sand pipe, the upper end of the washing machine is connected with the washing water outlet pipe, a central sand lifting tube to filter the sand to the sand washer of washing. The continuous flowing sand filter device is widely applied to industrial recycling water, deep treatment recycling technology for municipal sewage and water and so on.
NOVELTY - The utility model claims a straw synchronous enzymolysis ferment fuel ethanol reactor, the reactor comprises a mechanical stirring ferment tank, an air purifying device, a generating device, a temperature control system, a distillation tower, a computer control system and an upper computer monitoring system, a speed regulator and a stirring motor, a pressure pump, a ceramic ultra-filtration membrane separating device, the upper end is connected with the feedback input of mechanical stirring ferment tank, and the lower end is connected with the fermentation residue outlet at the lower end of the pressure pump is connected with the mechanical stirring ferment tank. A reactor integrating sterilization, enzymolysis and fermentation in one body, which not only can be used for straw synchronous enzymolysis fermentation production of fuel ethanol, but also can be used for straw fractional enzymolysis, fermentation technique for producing fuel ethanol, ceramic ultra-filtration membrane separating device can realize cellulase, repeatedly and circularly using the yeast, the reactor not only can be used for straw enzymolysis to ferment fuel ethanol production, but also can be used for fermentation of antibiotics, amino acids, enzymes and other biological product production.
NOVELTY - Compost exhaust purifying water ecological system, comprises: a compost reactor, a gas flow meter, a data collecting integrated module, gas on-line monitoring device, tail gas storage tank, a gas distribution system, diatomite, carbon dioxide adsorption tank, and a gas discharge device.    USE - Compost exhaust purifying water ecological system (claimed).    ADVANTAGE - The system improves water quality, and promotes ecosystem reproduction and growth.    DETAILED DESCRIPTION - Compost exhaust purifying water ecological system, comprises: a compost reactor, a gas flow meter, a data collecting integrated module, gas on-line monitoring device, tail gas storage tank, a gas distribution system, diatomite, carbon dioxide adsorption tank, a gas discharge device, compost reactor orderly connected with a gas flow meter, a gas line is connected to the monitoring device with the data collecting integrated module is on-line monitoring device, tail gas and carbon dioxide adsorption tank, a gas flow meter and a gas, a gas distribution system, diatom in the adsorption tank, a carbon dioxide adsorption tank with the gas discharge device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a compost exhaust purifying water ecological system.    Compost reactor (1)    Gas flow meter (2)    Collecting integrated module (3)    Gas on-line monitoring instrument (4)    Tail gas storage tank (5)    Gas distribution system (6)    Diatomite (7)    Carbon dioxide absorbing tank (8)    Fish (9)    Gas discharge device (10)
NOVELTY - A Penicillium lanosum 2-10-2 No. 110411-1 used for decomposing cellulose and lignin in straw, is new.    USE - The P. lanosum 2-10-2 No. 110411-1 is used for decomposing cellulose and lignin in straw (claimed).    ADVANTAGE - The strain has improved degradation efficiency.
NOVELTY - A Rhizomucor miehei lipase Pro-RML comprising: (a) SEQ ID NO. 2; or (b) SEQ ID NO.2 with substitution, deletion, or addition of an amino acid sequence, is new.    USE - The Rhizomucor miehei lipase Pro-RML is useful for hydrolyzing triacylglycerol and for producing biodiesel (claimed).    ADVANTAGE - The Rhizomucor miehei lipase Pro-RML can has higher triacylglycerol hydrolysis capability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a gene encoding the Rhizomucor miehei lipase Pro-RML; (2) a recombination vector comprising the gene; (3) a host cell comprising the recombinant vector; and (4) a method for preparing Rhizomucor miehei lipase Pro-RML.
NOVELTY - Livestock and poultry house ecological environment repairing agent comprises Lactobacillus, Bacillus, photosynthetic bacteria according to viable count ratio of 4-5:3-4:1, where repairing agent containing beneficial microorganism viable count is more than 108 CFU/mL.    USE - As livestock and poultry house ecological environment repairing agent (claimed), used for ecological bacteria.    ADVANTAGE - The livestock and poultry house ecological environment repairing agent makes the content of ammonia in barn air is reduced by 30%, at the same time, it can effectively prevent the harmful microorganism, reduces the incidence, and poultry environment repairing agent is safe and practical.
NOVELTY - The device has a chicken house provided with a belt transmission device that is connected with a chicken manure fermenting tank. The chicken manure fermenting tank and a chicken manure drying device are connected with a drying chicken manure part that is directly connected with a crusher, which is connected with a cattle feed and a marsh gas tank.    USE - Chicken cattle mixed feeding device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a chicken cattle mixed feeding device.
NOVELTY - Preparation of higenamine hydrochloride comprises taking 2-(3,4-dimethoxyphenyl) ethylamine as starting raw material, carrying out acylation cyclization reaction with 4-methoxy-phenylacetic acid, reducing, and deprotecting.    USE - Method for preparing higenamine hydrochloride (claimed).    ADVANTAGE - The method improves yield, shortens reaction route, reduces cost, and it is safe and environment-friendly.
NOVELTY - For one's electrolytic pole plate hydrogen-oxygen generator, this utility model relates to one for hydrogen and oxygen generator's cell pole piece, this utility model in order to solve the existing technology of 1, hydrogen and oxygen generator gas generating efficiency, large volume and high cost electrolytic cell, 2, electrolytic tank of hydrogen and oxygen generator air outlet is not smooth, 3, hot effect is not good, 4, easy short circuit's, said electrolytic pole piece is close to the periphery of rectangular plate is processed with a sealing installation groove, the lower end of side by side's rectangular plate is processed with multiple convex part, upper processing's rectangular plate is provided with at least one air outlet hole, the second pole piece separating fixed mounting hole and four first pole piece separating fixed mounting hole, two pole pieces isolated fixed mounting hole is vertically arranged, the pole piece separating fixed mounting hole's lower part is processed with a electrolyte circulating pump inlet pipe hole and electrolyte circulating pump outlet pipe hole, an electrolyte circulating pump outlet pipe hole and electrolyte circulating pump inlet pipe hole is horizontally arranged, the utility model is used in the hydrogen-oxygen mixed gas.
NOVELTY - An agricultural cycle system contains aquaculture system, planting system, livestock farming system, and biogas system in which aquaculture system, planting system, and livestock farming system are connected to each other, and planting system and livestock farming system are connected to biogas system in which biogas system contains biogas tank and biogas power generation illuminating lamp and biogas system is connected to biogas slurry conveyer which is connected to aquaculture system.    USE - An agricultural cycle system for fish ponds, field cultivation, and livestock breeding (all claimed).    ADVANTAGE - Agricultural cycle system is efficient and effective.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the agricultural cycle system. (Drawing includes non-English language text).
NOVELTY - A silver/titanium dioxide composite nanotube contains hollow titanium dioxide nanotube porous structure and distributed titanium dioxide nanotube on outer wall and inner wall of silver nanoparticle.    USE - A silver/titanium dioxide composite nanotube for lithium battery and hydrogen production.    ADVANTAGE - Product has uniform pore structure, improves electrode and contact area of electrolyte, and rapidly transports lithium ion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of silver (Ag)/titanium dioxide (TiO2) composite nanotube which involves formulating polyvinylpyrrolidone (PVP)/acetic acid solution of titanium complex viscous gel, preparing silver nitrate (AgNO3)/PVP/titanium composite solution of acetic acid, performing electrostatic spinning to prepare porous structure of Ag/TiO2 hollow tube, adding mineral oil to composite solution, stirring uniformly, performing electrostatic spinning to prepare TiO2 fiber, heating at rate of 2 degrees C/minute from room temperature to 500 degrees C, and performing heat preservation for 10 minutes.    DESCRIPTION OF DRAWING(S) - The drawing shows a scanning electron microscope image of silver/titanium dioxide composite nanotube.
NOVELTY - Preparation of organic biofertilizer comprises taking 8-15 pts. wt. biological bacteria, 900-1200 pts. wt. wheat bran, 15-30 pts. wt. brown sugar, 15-30 pts. wt. milk, 2-7 pts. wt. urea and 300-500 pts. wt. water, mixing, controlling humidity to 20-30%, stacking, covering with breathable material, fermenting at 45-50 degrees C, increasing temperature to 52-55 degrees C, adding 10-20 kg/ton biological bacteria and mixing.    USE - Method for preparing organic biofertilizer (claimed) used for improving soil quality.    ADVANTAGE - The product is environment-friendly.
NOVELTY - Preparation of organic biofertilizer comprises taking 0.02 wt.% Actinomycetes, 0.05 wt.% yeast, 0.02 wt.% Aspergillus and 0.02 wt.% Bacillus subtilis, mixing, adding 20-30 wt.% straw powder, mushroom, peanut shell powder, rice hulls or sawdust, carrying out aerobic fermentation at 15-20 degrees C for 48 hours, increasing temperature to 50-60 degrees C and at 75 degrees C, fermenting at 55-65 degrees C for 10-15 days, mixing, grinding, drying, pulverizing, crushing, sieving, filtering and packaging.    USE - Method for preparing organic biofertilizer (claimed).
NOVELTY - The method involves filling tetra-carbon and hydrocarbon in an aromatization reactor. The aromatization reactor is pre-heated for performing aromatization reaction operation. Dry gas, liquefied gas and liquid hydrocarbon are separated by a hydrocarbon product separation unit. The liquefied gas is filled into a butane unit. Dehydrogenation reaction is performed by an isobutene dehydrogenation reactor. Hydrocarbon feeding volume space velocity is about 0.1 to 10.0tT1.    USE - Method for mixing tetra-carbon and hydrocarbon aromatization production petrol with high octane blending component.    ADVANTAGE - The method enables ensuring better raw material cracking performance, yield petrol component blending efficiency and better economic benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for mixing tetra-carbon and hydrocarbon aromatization production petrol with high octane blending component. '(Drawing includes non-English language text)'
NOVELTY - An additive contains 15-25 pts. wt. emulsifying agent, 20-33 pts. wt. pH buffering agent, 8-12 pts. wt. tricresyl phosphate, 4-8 pts. wt. nitric acid isooctyl acrylate, 1-3 pts. wt. auxiliary emulsifying agent, 0.5-2 pts. wt. antioxidant, 13-20 pts. wt. organic solvent, and 18-26 pts. wt. isobutyl alcohol based on 100 pts. wt. additive in which pH buffering agent is composite mixture of 10-25 pts. wt. sodium petroleum sulfonate and 5-15 pts. wt. barium petroleum sulfonate, and organic solvent is aromatic hydrocarbon solvent, ketone solvent, ester solvent, and/or ether solvent.    USE - An additive used for blending fuel oil (claimed) such as blending modified methanol, blending methanol with oleic acid, blending methanol with other modified composite to prepare biofuel oil, blending biofuel oil with common petrochemical diesel oil, and blending all kinds of conventional condensate oil.    ADVANTAGE - Additive is environment-friendly, and improves cetane number, flash point, and corrosion resistance, and reduces pour point, cold filter plugging point, waste discharge, and cost of fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of additive which involves uniformly mixing 2 components of emulsifying agent to obtain 1st type component, completely dissolving antioxidant in organic solvent, mixing with nitric acid isooctyl acrylate to obtain 2nd type component, mixing pH buffering agent, tricresyl phosphate, and auxiliary emulsifying agent, heating, stopping when pH buffering agent is completely dissolved, cooling to less than or equal to 40 degrees C, adding isobutyl alcohol while continuously stirring, uniformly stirring to obtain 3rd type component, uniformly mixing 2nd type component and 3rd type component, adding 1st type component, and uniformly stirring.
NOVELTY - A purified methane is prepared from biogas by pretreating methane in booster system, sending to adsorption separating device, adsorbing, filling with adsorbent, separating methane from impurities, adjusting pressures, putting in storage tank, purifying methane, adsorbing, analyzing methane concentration, absorbing under vacuum pressure, separating methane from impurities, and discharging residual methane.    USE - Method for preparing purified methane from biogas (claimed).    ADVANTAGE - The method is simple.
NOVELTY - The utility model belongs to the technical field of cryogenic separation using liquid nitrogen cold energy one's with methane recovery function's liquid nitrogen washing device, comprising a liquid nitrogen pipe's refrigeration (P1), a high pressure nitrogen cooler (E3), a first raw material gas cooler (E4), a second raw material gas cooler (E5), a nitrogen washing tower for washing's (C1), flash tank (V1) and a rectifying tower's methane recovery (C2). The device can successfully for recycling liquid nitrogen washing's methane in the tail gas, and it has good economic benefit's, and the liquid nitrogen as cold energy, high working efficiency, energy-saving and environment-friendly, and the safety factor is high.
NOVELTY - A one are restorable alcohol The utility model claims's ether synthesis reactor, comprising a shell, a catalyst tube, hot exchange pipe and synthesis cavity, the shell's space surrounding a catalyst tube, hot exchange pipe, a catalyst cavity and synthesis cavity between the catalyst tube in the shell and synthetic cavity, hot exchange pipe is located by the synthesizing cavity's volume, synthesis cavity is provided with guide plate. The utility model's beneficial effects as follows: synthesizing alcohol ether fuel's heat generated can be hot exchange tube, has the function's constant reaction temperature, further, the guide plate's cavity can guide fluid toward the hot exchange tube direction, so the good's hot exchange, at the same time, increases the reaction substance remaining's time and improve the conversion rate's reaction.
NOVELTY - The method involves crushing corn straw. Crushed maize straw is mixed in a reaction kettle. Straw liquid is obtained under high temperature and high pressure of hydrogen. Solid-liquid mixture is filtered through a vacuum pump. Insoluble solid and organic liquid are separated. Insoluble solid adding acetone is filtered to obtain acetone solution. Organic liquid is distilled to obtain biomass fuel. Acetone solution is distilled to obtain acrylamide water solution without tar. Insoluble acetone is dried to obtain residue.    USE - Corn straw hydrogenation liquefaction process based biomass fuel preparation method.    ADVANTAGE - The method enables converting the corn straw into biomass fuel. The method enables storing and transporting the fuel in a convenient manner and avoiding generation of environmental pollution while burning the corn straw.
NOVELTY - The method involves processing a biodiesel crude product by an alcohol reclaiming tower. Monohydric alcohol is collected at a top part of the alcohol reclaiming tower. Alcohol and biodiesel crude products are separated by a kettle tower. Crude ester is refined by an ester distillation-tower. Gas collected at a top part of the ester distillation-tower is condensed to obtain biological diesel oil, where a condensation process is carried out in a hot exchanger. A least part of alcohol is reclaimed by the alcohol reclaiming tower.    USE - Method for refining biological diesel oil.    ADVANTAGE - The method enables coupling the alcohol reclaiming tower and the ester distillation-tower to save a hot source and a cold source, so that energy consumption of a biodiesel production process is effectively reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a biological diesel oil refining method.
NOVELTY - The furnace has a furnace body (1) formed with a fuel gas output opening. An air inlet device is provided with an air inlet pipe (4) that is connected with a jet device. The jet device is provided with an air nozzle (5). An air nozzle cover (6) is formed with air outlet holes. The air nozzle is connected with the air nozzle cover. The furnace body is arranged with an ash layer (12) and connected with a feeding port (2). The feeding port is matched with a furnace cover (11). An air nozzle air outlet hole is connected with a jet nozzle cover air outlet hole.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace ensures high ventilation effect so as to improve biomass oxidation rate, biomass gasification transform rate and biomass gasification fuel gas quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace body (1)    Feeding port (2)    Air inlet pipe (4)    Air nozzle (5)    Air nozzle cover (6)    Furnace cover (11)    Ash layer (12)
NOVELTY - Preparation of biomass fuel raw material comprises pulverizing biomass, and carbonizing; adding biomass waste to shredding machine, coarse crushing, fine crushing to remove ferrous metals, and removing and stone through air separator; adding to carbonization device, introducing generated volatile gases and waste biomass to combustion furnace to carry out combustion, and feeding high-temperature gas to carbonization device through fan as heat source; and fine crushing or grinding into particles, cooling, granulating through low-pressure steam, and adding liquid or powder, and molding.    USE - Method for preparation of biomass fuel raw material (claimed).    ADVANTAGE - The high-efficiency method achieves continuous and automated production of material.    DETAILED DESCRIPTION - Preparation of biomass fuel raw material comprises pulverizing biomass, and carbonizing; adding biomass waste to shredding machine, coarse crushing, fine crushing to remove ferrous metals, and removing and stone through air separator; adding to carbonization device to participate in carbonization process, introducing generated volatile gases and waste biomass to combustion furnace to carry out combustion, and feeding high-temperature gas to carbonization device through fan as heat source; and fine crushing or grinding into particles, cooling, granulating through low-pressure steam, and adding liquid or powder, and molding.
NOVELTY - Preparation of biomass fuel nut shell comprises crushing nutshell, sieving in over 50 mesh sieve, drying, adding 1-4C polyol solvent oil, stirring, molding for 4-8 hours, packaging, and transporting.    USE - Method for preparation of biomass fuel nut shell (claimed).    ADVANTAGE - The method ensures complete combustion with higher rate, avoids generating black smoke, and has convenient molding.
NOVELTY - A biomass fuel is prepared by crushing biomass to 100 mesh, adding organic solvent, stirring, reacting via cation exchanger and anion exchanger, reacting with potassium and chloride ions, adding 4-9C alcohols, gelatinizing starch, stirring, and molding.    USE - Method for preparing biomass fuel (claimed).    ADVANTAGE - The method extends life of boiler.
NOVELTY - A biomass briquette comprises 30-50 pts. wt. sawdust powder, 30-40 pts. wt. straw, 10-15 pts. wt. coal and 5-10 pts. wt. clay.    USE - Biomass briquette.    ADVANTAGE - The briquette is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biomass briquette comprising crushing waste wood to 50 mesh sawdust powder and coal to 40 mesh, standing, air drying straw, crushing, and drying straw to 6-8 mm length, and mixing with clay.
NOVELTY - A biomass fuel from nutshell comprises 6-12 pts. wt. 1-4C monohydric alcohol, 2-4 pts. wt. solvent and balance nutshell.    USE - Biomass fuel from nutshell.    ADVANTAGE - The biomass fuel has high calorific value.
NOVELTY - A biomass fuel comprises 35-50 pts. wt. cow manure, 20-35 pts. wt. dry pulverized coal, 8-15 pts. wt. deodorant and 0-22 pts. wt. loess. Deodorant comprises 17-25 pts. wt. bentonite, 6-13 pts. wt. zeolite powder and 3-5 pts. wt. potassium permanganate.    USE - Biomass fuel.    ADVANTAGE - The fuel is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel comprising mixing raw materials, and pressing.
NOVELTY - Biomass fuel comprises 50-75 wt.% straw, 15-30 wt.% 4-9C alcohol, 1-4 wt.% solvent, 10-20 wt.% starch, and 2-4 wt.% potassium-removing agent.    USE - Biomass fuel.    ADVANTAGE - The fuel results to efficient combustion process and long service life of boiler.
NOVELTY - A biomass fuel is prepared by crushing raw materials, sieving, adding organic solvent, stirring, performing cation exchange, adding 4-9C alcohol and starch, stirring, and molding.    USE - Method for preparing biomass fuel (claimed).    ADVANTAGE - The method results to fuel that prolongs boiler service life.
NOVELTY - Biomass fuel comprises 50-75 wt.% straw, 15-30 wt.% C4-C9 alcohol, 1-4 wt.% oil solvent, 10-20 wt.% starch, 2-4 wt.% potassium-removing agent and 2-4 wt.% dechlorinating agent.    USE - Biomass fuel.    ADVANTAGE - The fuel prolongs the boiler service life.
NOVELTY - The system has a reservoir (2) whose lower portion is provided with discharge port (6) at the valve (4). The aluminum-base composite is provided into reactor (9) for generating hydrogen output through the hydrogen outlet (11). The gas pipe (24) from gas valve (29) is entered into stainless steel tank (19). The gas is passed through the hydrogen storage alloy (23). A thermoelectricity semiconductor element (26) is installed on hot ring (25), and bypass branch in parallel with steel tank. The hot ring and radiating frame together generate electric energy stored in the storage battery.    USE - Integrated hydrogen storage power generating system.    ADVANTAGE - The device with simple manufacturing process, easily controllable process, low cost, environment-friendly effect, energy-saving effect and convenient use can be obtained. The hydrogen production process is easy to control, and the device is convenient to install and use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated hydrogen storage power generating system.    Reservoir (2)    Valve (4)    Discharge port (6)    Reactor (9)    Hydrogen outlet (11)    Stainless steel tank (19)    Hydrogen storage alloy (23)    Gas pipe (24)    Hot ring (25)    Gas valve (26)    Gas valve (29)
NOVELTY - This utility model claims one kind of biological desulphurization device, comprising an absorption tower, a bioreactor and centrifugal separator, the raw material gas from the lower part's absorption tower, the tower top liquor spray device founction's alkali solution counter-current contact to remove H2S in the gas's, an absorption tower 1 exhaust port's discharge purified gas after gas-liquid separation device for filtering liquid to the subsequent processing stage. The bottom of the absorption tower discharge opening's sulfur-containing liquid enters into reactor, the air blower in the bioreactor, and regenerated alkali liquor through the pipeline's return to the alkali liquid spray device's through the alkali liquor absorbing tower's sulfureted hydrogen and carbon dioxide in marsh gas, by use of bioreactor in the culture's efficient aerobic bacteria removing hydrogen sulphide, the regeneration cycle. Process chain is short, the device is simple, the operation and maintenance is convenient.
NOVELTY - This utility model claims one kind of ultra-pure ammonia water production system, comprising a liquid ammonia tank, pre-treatment tank, super-pure water tank, decompressing and distilling device, a semi-finished product tank one, a semi-finished product tank, pure water tank, filtering system, a finished product tank. The utility model super-pure water tank by the super-pure water into the pre-processing tank, liquid ammonia by the ultrapure water taking water washing, can effectively remove metal ion impurities and non-metal ion impurities so as to avoid secondary pollution, filtering system using partial multiplex technology of multi-stage film circular filtering system can remove the diameter of more than 0.5 (mu) m, the purity reaches PPT, the large scale integrated circuit production process to make the localization, .
NOVELTY - The utility model claims the terpineol production's suitable for waste water recycling system, comprising a water device, said water device is connected with the storage tank and boiler, turpentine oil turpentine oil storage tank is connected with said water collection unit production, said production unit is connected with production water collecting pool, said collecting basin production and turpentine oil tank is connected, at the same time, said boiler is connected with sewage collecting unit, said sewage collecting unit is connected with sewage collecting pool, sewage processing pool is connected with said one group of water pump, said water pump is connected with the boiler. The utility model improves the production's structure and fully taking's waste water recycling, reduces the waste water discharge, which directly reduces the waste water processing cost, which is good for improving the efficiency of whole production's, but also helpful for protecting's surrounding environment and has better's.
NOVELTY - An automatic one poultry and livestock manure target turning machine, comprising a manure fermenting bed's case upper two sides of the poultry and livestock, and in the box's power machine, one main shaft and one transmission shaft of the power machine is equipped with the reduction box and controller, the reduction box is linked to the main shaft, up through the first and second transmission gear or a transmission chain/chain wheel, the linkage's turning to the turning rake teeth and rake teeth shaft up to make one's turning rake teeth in the rows fermenting bed up . Operation time, but also can through the hand rocking handle rotating one inner thread screw to drive the arm, an adjusting turning rake teeth shaft up and down, drives the row's rake teeth downwards gradually deeply turning, horizontal turning to moderate to the target depth , or reverse. The utility model turning target machine, automatic walking, body is thin, depth can be adjusted, high power, high efficiency, good leak tightness is good, and it saves labour and is suitable for poultry and livestock manure processing poultry and field's proliferation.
NOVELTY - This utility model claims one kind of heating continuous wastewater treatment system of biological carbon complete equipment, belonging to the technical field of renewable energy source. The technical solution comprises feeding hopper (2), continuous carbonizing furnace (7), operation platform (17) and three-way discharge hole (13), operation platform (17) and the middle part carbonizing device main body (7) upper part and the crane (17) connecting, the top part is equipped with material active compacter (6), and the lower part are uniformly distributed around the detecting detection hole (9), three-way discharge hole (13)'s upper part and the continuous carbonizing furnace (7)'s distributor (19) connecting. In the raw material by the carbonization furnace feeding hopper, inner wall of the furnace temperature, start the pyrolysis reaction to generate's bio-char is downward conveying furnace body. The utility model solves the problem that the biomass carbon production in the process of raw material feeding is not smooth, carbonization is not enough and so on, improves the production efficiency, is suitable for different biomass raw material's. The utility model promotes the development of our country's bio-char industry;
NOVELTY - This utility model claims one kind of kiln type marsh gas dry fermentation device, separated by a circular fermentation room's kiln type fermentation room, said's kiln type fermentation room is composed of one circular fermenting space radially from the center of a circle is divided into 4 or 6's is formed between the circular edge and circular fermentation between outer ring is annular; upper dome is equipped with marsh gas storage's gas storing each kiln type fermentation between the top part and the upper dome's air bag between left vent hole, a sealing film is equipped with an elastic upper the feeding port, the outer side of each wheel's type fermentation kiln is installed with a discharging door, for conveying the fermenting marsh gas accumulation's gas collecting pipe in each kiln type fermentation room, between the circular fermentation base peripheral water outlet, ,'s of fermentation liquor recycling system. The utility model can completely solve farm livestock and poultry excrement and crop straw pollution and realizes resource utilization of agricultural waste, the agricultural waste are converted into clean energy and non-polluted organic fertilizer, agricultural waste to realize zero discharge.
NOVELTY - Circular mold granulator comprises main machine (1), liquid tank (2), powder box (3), feeding screws, displacement pump (6), and quenching and tempering machine (7).    USE - Circular mold granulator.    ADVANTAGE - The granulator has quantitatively accurate liquid adding device, increased uniformity, high grain quality, reduced forming resistance, reduced energy consumption, and improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation of circular mold granulator comprising cutting raw material, screening, grinding, screening, drying, grinding oversize, adding liquid, stirring, quenching, tempering, granulating, cooling, screening, and crushing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of circular mold granulator.    Main machine (1)    Liquid tank (2)    Powder box (3)    Displacement pump (6)    Quenching and tempering machine (7)
NOVELTY - This utility model claims a kind of plasma de-hydrogen high efficient and energy saving boiler, wherein the boiler body is set with a fan, a furnace chamber, a furnace door, feeding door, fire arrestor, a low temperature plasma generator, high frequency high voltage power supply, a switch, a steam pipeline is provided with hydrogen and oxygen injection pipe in the boiler hearth. High frequency high voltage power supply is connected with the low temperature plasma generator, a low temperature plasma generator is connected with flame arrester, fire arrestor is connected with the injection pipe, and the other end of the spraying tube is installed in the boiler hearth, one end of the steam pipe is connected with the top end of the furnace, the other end is connected with a switch. This utility model is the boiler to generate the first part of the steam, carrying out electrochemical activation of the low temperature plasma generator can be decomposed into hydrogen and oxygen and hydrogen ions, oxygen ions to fully burn, then sent to the hearth and a fuel combustion together, it can save 30%, improve the effect of reducing a 40%, industry, civil boiler industry for an update of a new product, and the market prospect is very wide.
NOVELTY - This utility model claims a plant straw extruding cracking biological oil production device. It comprises a driving device and a material extruding screw rod, a material extruding screw periphery is provided with the cylinder, the periphery is provided with a combustion chamber, the combustion chamber is provided with a fuel gas heater, cylinder close to one side of the drive device is provided with thickened; Screw cylinder and integrally connected, the centre of the Screw auger is provided with a connecting rod, connecting rod is provided with a packing auger blade, Screw lower part is provided with a self-closed slag. Screw is set on the upper part oil outlet pipe, the oil outlet pipe is connected with an oil-gas separator, an oil-gas separator is connected with a conveying pipe, the tail end of the conveying pipeline is connected with a compressed gas storage tank. The advantages lie in: replace the bituminous coal to heat the straw cracking, which reduces the pollution to the atmosphere environment, at the same time recycling the dry gas can be a combustible gas can be used as fuel gas for fuel gas heater, so as to avoid the dry gas caused by discharging air secondary pollution and reaches the effect of saving energy.
NOVELTY - This utility model claims a biomass thermal cracking system, a feeding device and a drying system, the drying system is connected with the separation system connected with, a separation system and the zero negative-pressure conveying system connected with the zero negative-pressure conveying system and burning system. Drying system comprises a chain conveyer, a heating pipe, separating system is connected with a chain conveyor for rolling sieving machine, a motor is connected with the rolling screen connected with the gravity machine, zero negative-pressure conveying system comprises a biomass is connected with the gravity machine discharge hole of zero negative pressure conveyer, a biomass is connected with zero negative pressure conveying a level of biomass in the negative pressure conveyer, the biomass zero negative pressure conveyer outlet fine crusher, burning system comprises a pyrolysis furnace, pyrolysis furnace is connected with the fine crusher. This utility model is used for household garbage processing, does not produce toxic substance, environment protection and high efficiency.
NOVELTY - The system has a set of turbo expanders (19, 20) connected to an after cooler (12). A set of refrigerant heat exchange unit (31) is connected to a first of a set of refrigerant compressors (11, 13) and a last of the set of turbo expanders, such that all components form a close refrigeration cycle. A main cryogenic heat exchanger (3) facilitates heat exchange between pressurized natural gas passing through a natural gas liquefaction subsystem and a refrigerant passing through a refrigeration subsystem such that the pressurized natural gas is liquefied by the refrigerant.    USE - Liquefied natural gas (LNG) production system.    ADVANTAGE - The system allows the refrigerant stream to be split after first of the turbo expanders distribute cold energy according to heat demand for the natural gas liquefaction as the cold energy is required for the condensing service at intermediate temperature than the sub-cooling for the natural gas at low temperature, such that the temperature difference between the cold and warm streams is evenly approached along the heat flow by changing the natural gas feed pressure, thus improving efficiency and specific power requirement of the system with low refrigerant flow rate requirement and low expansion ratio requirement. The turbo expanders are arranged in series, thus operating the system in a simple and flexible manner.    DETAILED DESCRIPTION - The main cryogenic heat exchanger is a multi-stream heat exchanger, and the refrigerant is nitrogen. An INDEPENDENT CLAIM is also included for a method for producing liquefied natural gas by a single phase gaseous refrigerant in a close loop.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a LNG production system.    Main cryogenic heat exchanger (3)    Refrigerant compressors (11, 13)    Coolers (12, 14, 16, 18)    Turbo expanders (19, 20)    Refrigerant heat exchange unit (31)
NOVELTY - Lignocellulosic biomass is subjected to enzymatic saccharification process by processing pre-processed lignocellulosic biomass by lignin degradation enzyme, subjecting biomass processed by lignin degradation enzyme to enzymatic saccharification process, separating and recovering reaction product and enzyme-containing liquid from suspension produced at enzymatic saccharification process, and circulating recovered enzyme as enzyme for enzymatic saccharification process.    USE - Enzymatic saccharification of lignocellulosic biomass for manufacture of ethanol.    ADVANTAGE - Separation or recovery of saccharogenic amylase from enzyme treatment suspension can be easily performed, enzyme loss can be suppressed, and high circulation ratio of saccharogenic amylase in enzymatic saccharification treatment process can be maintained over a long period of time.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of enzymatic saccharification of lignocellulosic biomass. (Drawing includes non-English language text).
NOVELTY - A process for producing biodiesel under subcritical condition is provided. In said process, the materials comprising neutral lipid, water, and methanol are added in a reactor, followed by increasing reaction temperature higher than about 100 DEG C but lower than about 240 DEG C and pressure so that the solution in the reactor is kept under subcritical condition. After an appropriate reaction time, biodiesel is obtained.
NOVELTY - The system has a suction fan which is mounted onto cooling chamber. A gas filtration and steam condensation chamber is provided with a tank got receiving fresh water and condensation water for gas filtration. The alternatively placed perforated steel floors are used for the condensation of steam contained in the cooled gas. A water level equalizer pipe is interconnected with bottom discharge valve of the gas filtration and steam condensation chamber, and a self-draining valve is mounted on the pipe.    USE - Biomass gasification system.    ADVANTAGE - The system can be operated efficiently within short gasification time, without causing smoke and clogging the pipeline or gas-regulating valve.
NOVELTY - Biologically preparing epoxy biodiesel lubricating base oil, involves: (1) ultrasound-assisted heat and mass transfer ring-opening isomerization etherification reaction; and (2) bleaching the product obtained in (1) to obtain a clear and transparent biological lubricating base oil.    USE - The method is useful for biologically preparing epoxy biodiesel lubricating base oil (claimed).    ADVANTAGE - The method uses a catalyst with high selectivity.    DETAILED DESCRIPTION - Biologically preparing epoxy biodiesel lubricating base oil, involves: (1) ultrasound-assisted heat and mass transfer ring-opening isomerization etherification reaction: mixing long-chain fatty alcohols and metal ion supported cation exchange resin catalyst and heating to a certain reaction temperature, adding an epoxy ring-opening reaction of biodiesel, the reaction is stopped when the epoxy value is less than 0.1, the reaction mixture is cooled to room temperature, washing with distilled water, separating the lower aqueous phase and recovering the solid catalyst, the upper organic phase is then washed until neutral, and vacuum dehydration, finally obtaining light components isomerized oil ether; and (2) bleaching the product obtained in (1) to obtain a clear and transparent biological lubricating base oil.
NOVELTY - Fatty acid alkylester is manufactured by reacting free fatty acid-containing oil and monovalent lower alcohol in the presence of acidic catalyst using alcohol as solvent to obtain fatty acid alkylester with free fatty acid, recovering water, unreacted alcohol, and acidic catalyst in the lower part of the reaction liquid, and reacting oil which does not contain free fatty acid and linear alcohol with less than or equal to 2 carbon number in the presence of an alkali catalyst fatty acid alkylester oil.    USE - Manufacturing method of fatty acid alkylester for biodiesel fuel.    ADVANTAGE - Special removal process for acidic catalyst is not required, separation of water and oil is easy and fast, temperature condition is low, reaction duration is short, yield is high, and waste is reduced.
NOVELTY - The system (1) has a fine powder fuel manufacturing equipment (10) equipped with a belt conveyor. The fine powder fuel manufacturing equipment manufactures fine powder fuel. The fine powder fuel is burned to produce electric power by utilizing heat energy. An energy conversion part (20) is equipped with a gasification facility (21) and a coal-fired-power-generation installation part (27). The energy conversion part liquefies the fine powder fuel to generate reformed fuel. A supply part supplies generated electric power to a consumer installation part (30).    USE - Heat energy supplying system for use in a coal-fired power plant.    ADVANTAGE - The supply part supplies generated electric power to the consumer installation part so as to accelerate utilization of the fine powder fuel by using an existing facility of a consumer and biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a heat energy supplying system.'(Drawing includes non-English language text)'    Heat energy supplying system (1)    Fine powder fuel manufacturing equipment (10)    Energy conversion part (20)    Gasification facility (21)    Coal-fired-power-generation installation part (27)    Consumer installation part (30)
NOVELTY - Propagating ethanologen from biomass comprises: (a) providing a medium for propagation of ethanologen; (b) supplying a first cell mass of ethanologen to the medium; (c) supplying xylose or a component obtained from the biomass to the medium as a carbon source for cell mass growth of the ethanologen; and (d) maintaining the medium comprising the first cell mass of ethanologen at a pH of 5-6 and at 26-37 degrees C so that the first cell mass of ethanologen is propagated into a second cell mass of ethanologen, where the second cell mass of ethanologen is larger than the first cell mass of ethanologen.    USE - The method is useful for propagating ethanologen, which is useful for producing a fermentation product (claimed) e.g. beer.    ADVANTAGE - The method provides the fermentation product at high yield with high conversion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for propagating ethanologen from biomass in a fermentation system, comprising a first stage comprising a first vessel configured to maintain a medium comprising ethanologen, a second stage comprising a second vessel configured to maintain a medium supplied from the first stage, a source of xylose to be provided to the medium as carbon source for ethanologen in the first stage, and a source of xylose to be provided to the medium as carbon source for the ethanologen in the second stage, where the ethanologen has a first cell mass when supplied to the first stage and the ethanologen has a second cell mass when supplied from the first stage to the second stage and the ethanologen has a third cell mass when supplied from the second stage, the second cell mass is at least 200 times larger than the first cell mass, and the third cell mass is at least 20 times larger than the second cell mass.
NOVELTY - Producing a carboxylate ester from a renewable resource, comprises providing a water soluble carboxylate, providing a transfer agent, removing water, if present, providing a di-alkyl carbonate, and reacting the carboxylate, transfer agent and di-alkyl carbonate to form a di-alkyl ester of the carboxylate, and a carbonate, substantially in the absence of water.    USE - The method is useful for producing a carboxylate ester (claimed), which is useful for producing polymers.    ADVANTAGE - The green process produces highly pure carboxylate ester with high yield by minimizing the use of chemicals and energy, in a cost effective and industrial manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the carboxylate ester obtainable by the above process.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for producing dimethyl succinate.    Bioreactor (101)    Carboxylate anion exchanger (104)    Purification unit. (107)
NOVELTY - Method (M1) of continuous liquid fuel production utilizing biomass involves receiving at least one biomass feedstock; utilizing first portion of biomass feedstock to produce synthesis gas from first thermochemical process; utilizing second portion of biomass feedstock to produce bio-oil from second thermochemical process; and generating liquid fuel by combining the produced synthesis gas and produced bio-oil.    USE - For continuous production of liquid fuel such as diesel from biomass (claimed), and for energy production; and to produce other product streams including electrical power generation and/or biochar.    ADVANTAGE - During the biomass processing, the system runs at atmospheric pressure to very slightly positive pressure of up to 10 torr, which serves to minimize leaks in the system and significantly reduces the risk of an escalating pressure event. The process for conversion of cellulosic biomass into hydrogen may enhance the recycling of cellulosic biomass products and turn its waste into power generation. The waste of cellulosic biomass includes forest floors that currently are not economical to recover, but present a serious fire hazard. By recycling the cellulosic biomass waste through the use, the hazard problem may be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (S1) for continuous liquid fuel production from biomass comprising first reaction chamber configured to produce synthesis gas from first biomass stream; second reaction chamber configured to produce bio-oil from second biomass stream; and an enrichment chamber configured to receive the produced synthesis gas and produced bio-oil from the reaction chambers and enrich the produced bio-oil with the produced synthesis gas to produce liquid fuel.
NOVELTY - Fuel composition comprises: a diesel base fuel; 1-10 vol/vol.% a fatty acid alkyl ester; and more than 10 vol/vol.% ether component, where the ether component comprises at least one ether compound (I) having 8-12C.    USE - Used as fuel composition.    ADVANTAGE - The fuel composition: has a measured cetane number of greater than or equal to 40 (claimed); exhibits minimal transfer into engine sump and cause minimal dilution of lubricant and increased bio-fuel component, thus lubricant performance properties such as protection and durability are not effected; requires lower level of cetane boost additives, thus reducing cost and complexity of preparing the composition, and/or provides greater versatility in fuel formulation practices; and boosts cetane number with or without fatty acid methyl ester component.    DETAILED DESCRIPTION - Fuel composition comprises: a diesel base fuel; 1-10 vol/vol.% a fatty acid alkyl ester; and more than 10 vol/vol.% ether component, where the ether component comprises at least one ether compound (I) having 8-12C.    R1, R2 = primary or secondary alkyl.    An INDEPENDENT CLAIM is also included for increasing the concentration of a bio-fuel component in a diesel fuel composition comprising blending more than 10 vol/vol.% (I).
NOVELTY - Producing mixed esters of fatty acids, comprises partially transesterifying a mixture of fatty acid methyl ester with at least one 2-8C-alkyl alcohol in the presence of a heterogeneous solid acid catalyst at 50-200 degrees C and a pressure of 0.5-20 atmosphere to produce a mixture of fatty acid alkyl esters including at least some fatty acid methyl esters and fatty acid alkyl esters with alkyl group having 2-8C, where the mixture of fatty acid methyl ester is free from fatty acid alkyl ester with alkyl ester group, and separating the mixture of fatty acid alkyl ester from the acid catalyst.    USE - The process is useful for producing mixed esters of fatty acids (claimed), which is useful as biofuels for compression ignition engine.    ADVANTAGE - The continuous and improved process produce biofuels, which is renewable, non-toxic and biodegradable fuel alternative, with improved fuel economy, horsepower and torque, and superior lubricity. The biodiesel provides a substantial reduction of emission of unburned hydrocarbons, carbon monoxide, and particulate matter, and is free of major pollutants, such as sulfur and aromatics.
NOVELTY - Manufacture of biodiesel involves adding methanol, and calcium carbonate or limestone into vegetable oil or waste vegetable oil, calcining resulted product using porous catalyst at 1000-1200 degrees C under atmospheric pressure for 2 hours, and maintaining at 70-100 degrees C. The weight ratio of methanol and waste vegetable oil is 6:1-9.3:1.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The method enables manufacture of biodiesel with high productivity without producing acidic or basic byproduct.
NOVELTY - A catalyst is a mixed metal oxide catalyst comprising 10-40 wt.% group VIII metal, 5-30 wt.% trivalent metal, 0.1-8 wt.% group IA metal, 0.1-8 wt.% group IVB metal, 0.1-30 wt.% group IIB metal, 5-50 wt.% two group VIB metals (all based on oxide conversion) and 10-30 wt.% silicon dioxide-aluminum oxide. The content of silicon dioxide in silicon dioxide-aluminum oxide is 90-99 wt.%. The molar ratio of two group VIB metals is 3:1-1:3. The catalyst has specific surface area of 150-300 m2/g and pore volume of 0.4-0.8 ml/g.    USE - Catalyst is used for selective hydrogenation of diene e.g. 4-8C conjugated diene (all claimed).    ADVANTAGE - The catalyst has excellent durability, and high activity and selectivity with respect to diene even at low reaction temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of catalyst; and    (2) application of catalyst in selective hydrogenation of diene.
NOVELTY - Pretreated product of lignocellulosic biomass for saccharification, in which lignin is dissociated from the substrate or the substrate is swelled, obtained by pretreating the lignocellulosic biomass as a substrate before saccharification, where 60-80% of all pores of the substrate have a diameter of 10-50 nm, is claimed.    USE - The pretreated product of lignocellulosic biomass is useful for saccharification of saccharified solution containing saccharides such as glucose, xylose and arabinose to produce bioethanol that is mixed with gasoline for automotive fuel.    ADVANTAGE - The pretreated product of lignocellulosic biomass is capable of efficiently providing the saccharified solution with uniform quality regardless of the lignocellulosic biomass quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the pretreated product of lignocellulosic biomass, comprising (a) maintaining a substrate mixture, obtained by mixing the substrate and ammonia water, at a predetermined temperature for a predetermined period of time to separate at least a part of hemicellulose having a molecular weight of 7.8x 103 to 2x 106 and composing the substrate, and (b) forming pores in the substrate while adjusting the pores of the substrate.
NOVELTY - A biodiesel composition (C1) comprises 4.5-95.5% of first 2-13 centistoke polyalpha olefin; 95.5-4.5% of second 2-13 centistoke polyalpha olefin; 4.5-5.5% polyolefinic ester; 4.5-80.5% calcium overbased sulfonate; and 19.5-20.5% bean or seed oil, where the first and second polyalpha olefins have different centistokes values and where particle size of calcium is 50-100 Angstrom .    USE - As fuel additive used in diesel, biodiesel, jet fuel, bio jet fuels (claimed), engine oils, other types of fuels or oils and lubricants.    ADVANTAGE - The composition has shelf life of at least 9 months. The composition will not freeze up to temperature of -33 degrees F. Addition of the biodiesel composition to diesel, biodiesel, jet fuel or bio jet fuels lowers the cloud point by 10 degrees F (preferably at least 25 degrees F); and reduces carbon emissions by 10% (preferably by at least 14%).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) of making biodiesel fuel additive composition involving mixing the components of (C1) at 76 degrees F and stored at 72 degrees F; and    (2) method (M2) of using biodiesel fuel additive composition involving adding composition (C1) into fuel tank of engine; and running the engine.
NOVELTY - The apparatus has a de-waterer material exit port fixed into a process drum assembly (2) through an opening in an entry endplate (4). An exit conveyor (17) carries finished pellets up to a machine exit. A custom square-round adapter (20) joins a circulation blower (15) to a volatile organic compounds (VOC) filter box (18). An activated carbon filter is housed in the VOC Filter Box that is connected to a material separator assembly (14) by the square-round adapter. A sub-frame (13) supports components.    USE - Apparatus for reducing organic waste by rotary desiccation.    ADVANTAGE - The apparatus shuts off the circulation blower to prevent air from back- streaming through the pelletizer, reduces the landfill and compost waste streams by processing the waste at the site of generation, and automatically processes and sorts the organic wastes and contaminants with no intervention from operators and little maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows left and right sides perspective views of an apparatus for reducing organic waste by rotary desiccation.    Process drum assembly (2)    Entry endplate (4)    Sub-frame (13)    Material separator assembly (14)    Circulation blower (15)    Exit conveyor (17)    VOC filter box (18)    Custom square-round adapter (20)
NOVELTY - A molding containing baked biomass and coal are mixed. The material containing baked biomass and coal is pulverized, to obtain composite fuel.    USE - Manufacture of composite fuel used for manufacturing fuel for boiler and fuel for cement kiln.    ADVANTAGE - The method provides composite fuel which carries out stable combustion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for columnar molding.
NOVELTY - A fuel cell power generation system has a desulfurizing apparatus provided in a container such that raw fuel gas contacts desulfurizing agent absorbing sulfur compound, heater (21) heating desulfurizing agent at 50-200 degrees C while contacting raw fuel gas, and reformer (3) having hydrogen as main component and generating reformed gas reforming desulfurized raw fuel gas, where desulfurizing agent is zeolitic adsorption agent having zeolite as main component.    USE - Fuel cell power generation system (claimed).    ADVANTAGE - The fuel cell power generation system has excellent energy efficiency, and comprises desulfurizing agent having excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for desulfurizing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell power generation system. (Drawing includes non-English language text)    Reformer (3)    Fuel cell (6)    Heater (21)    Exhaust-heat collector (22)    Heater control unit (32)
NOVELTY - The LNG plant has a system that includes a unit (10) for performing a pressure swing adsorption process at high pressure for purification of feed natural gas (20). The pressure swing adsorption process removes carbon dioxide, hydrogen and other impurities from the feed natural gas and maintains the pressure of the feed natural gas for further processing in the LNG plant.    USE - Liquefied natural gas (LNG) plant.    ADVANTAGE - By performing the pressure swing adsorption process, the risks associated with the wet and hazardous chemicals of the amine absorption can be avoided and the need for recompression following a low pressure swing adsorption process can be eliminated. The efficiency of the LNG plant can be increased and the cost of equipment and operation can be lowered.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system used for performing pressure swing adsorption process.    Unit for performing pressure swing adsorption process (10)    Feed natural gas (20)    Product stream (30)    Recycle steam (40)    Tail gas (50)
NOVELTY - Absorbing acid compounds contained in a gaseous effluent, comprises contacting the gaseous effluent with an aqueous solution including at least one amine and at least one amine degradation inhibitory compound, selecting a corrosion resistant stainless steel when it is present in contact with the amine degradation inhibitory compound, and utilizing equipments whose surfaces contact with the aqueous solution are made of stainless steel.    USE - The method is useful for absorbing acid compounds, belonging to a group comprising carbon dioxide and hydrogen sulfide, contained in a gaseous effluent such as natural gas, flue gases, synthesis gas, refinery gas, gas obtained by Claus process, biomass fermentation gases, cement plant gas and fume incinerator (all claimed).
NOVELTY - A vitamin B2 fermentation waste liquid probiotic is prepared by adjusting vitamin B2 fermentation waste liquid pH to 5.5-7.2, adding probiotic bacteria strain which is 0.5% of total waste liquid weight, controlling temperature to 38-41 degrees C, fermenting until fermentation liquid pH is 5 or fermentation solution, mycelium, or spore content is 1x 1010 colony-forming unit (CFU)/g, carrying out enzymolysis of fermented liquid, centrifuging, collecting bacteria or spore, and drying mycelium or vacuum-drying spore.    USE - Preparation of vitamin B2 fermentation waste liquid probiotic (claimed).    ADVANTAGE - The preparation has short process flow, improves working efficiency, animal production performance, and ability to resist disease, saves production cost and culture medium preparation, is energy-saving, reduces emission, maintains nutrition value, promotes growth, and replaces use of antibiotics.
NOVELTY - A macroporous iron carbide catalyst contains iron carbide from carboxylic acid-modified polymethyl methacrylate microsphere as template and prepared ferric nitrate as precursor in which macroporous iron carbide catalyst has 50-1000 nm pore size.    USE - Macroporous iron carbide catalyst for biological synthesis of fuel gas (claimed).    ADVANTAGE - The catalsyt has simple and short preparation and low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of macroporous iron carbide catalyst which involves adding ferric nitrate to methanol/ethylene glycol mixed solution in which molar ratio ferric nitrate:methanol/ethylene glycol mixed solution is 1:1-3 and volume ratio methanol:ethylene glycol is 1:1.5-4, stirring to obtain ferric nitrate solution, adding carboxylic acid-modified polymethyl methacrylate microsphere, impregnating, filtering, drying, and heating to 400-800 degrees C for 4-8 hours; and    (2) application of macroporous iron carbide catalyst for biological synthesis of fuel gas containing hydrogen (H2), carbon monoxide (CO), carbon dioxide (CO2), methane (CH4), and nitrogen (N2) in 1:1:0.5-0.8:0.1:2-3 ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows a catalytic activity result of the iron carbide catalyst in biological synthesis of fuel gas. (Drawing includes non-English language text).
NOVELTY - An ammoniacal nitrogen fertilizer is prepared by washing poultry feather, sterilizing at 100-130 degrees C after drying crushed poultry feather to form feather meal, mixing feather meal, water and proteolytic enzyme in weight ratio of 100:50-80:0.2-0.5, subjecting mixture to thermostat enzymatic reaction at 40-60 degrees C for 2-4 days and controlling pH to 7-9, filtering undissolved feather to obtain ammoniacal nitrogen liquid and spray drying ammoniacal nitrogen liquid.    USE - Ammoniacal nitrogen fertilizer is used for soil for vegetable cultivation (all claimed).    ADVANTAGE - The ammoniacal nitrogen fertilizer is economically prepared with high yield, by simple method.
NOVELTY - A buparvaquone is prepared by dissolving 1,4-benzopyran dione and tert butyl cyclohexyl acetate in solvent 1, adding amine-based reagent, condensation reacting at 30-80 degrees C for 3-12 hours under inert gas to obtain (E)-2-(3-methylbutylidene) cyclohexanone derivative (I), crystallizing in organic solvent, dissolving in solvent 2 at 40-80 degrees C, vacuum drying, reacting under strong alkali condition, adding acid reagent to pH of 7-8, vacuum concentrating and crystallizing.    USE - Method for preparing buparvaquone (claimed).    ADVANTAGE - The method avoids expensive catalyst, improves product yield, is environment-friendly and easy to industrialized.
NOVELTY - Affixing carbon dioxide onto a surface of a material, comprises: (a) contacting a cellulosic material with a composition comprising an amino compound; (b) contacting the cellulosic material with a composition comprising a source of metal ions; and (c) contacting the cellulosic material with a composition comprising carbon dioxide.    USE - The method is useful for affixing carbon dioxide onto the surface of a cellulosic material (claimed), where the obtained cellulosic material is useful: as a fertilizer; as strengthening aid in plastics; as a filler in building materials; and for storing and/or transporting carbon dioxide. No biological data given.    ADVANTAGE - The method provides the cellulosic material, which: is stable at a temperature up to 50 degrees C (claimed); is efficient in capturing carbon from the atmosphere; can be transported in an easier and cost effective manner; does not release the carbon dioxide under normal climatic extremes of heat or cold or in very wet, very dry, windy or stormy environments; and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a cellulosic material which has been treated with the amino compound, the source of metal ions and carbon dioxide that is retained on its surface.
NOVELTY - Manufacturing biodiesel comprises either carrying out ester conversion reaction using biodiesel raw material and alcohol and sulfuryl halide under complex ester conversion catalyst, or mixing biodiesel raw material and sulfuryl halide containing methanol with microalgae fungi to obtain a mixed liquid, and carrying out ester conversion reaction under complex ester conversion catalyst.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The method: enables the free fatty acid or lipid content to be low; does not generate free fatty acid or moisture during reaction; is economical and has faster reaction rate; improves the yield and quality of the biodiesel in comparison with acid catalyst using methods; and progressively carries out reaction at a low temperature.
NOVELTY - The method involves collecting sludge or kitchen biogas residue and agriculture and forestry waste. 55-65 wt.% of water content is mixed to the collected waste and placed to a sealed horizontal double-layer tube aerobic fermentation tank, where primary aerobic fermentation process is performed at temperature of about 65 degrees Celsius to 75 degrees Celsius and secondary aerobic fermentation process is performed at temperature of about 50 degrees Celsius to 60 degrees Celsius. The mixed content is crushed and sieved to prepare organic fertilizer.    USE - Method for preparing biological organic fertilizer using municipal sludge or kitchen closed aerobic biogas residue.    ADVANTAGE - The method enables preparing organic fertilizer in a simple and economical manner, ensuring material ferment degree and uniform processing effect and high automation degree, performing primary aerobic fermentation and secondary aerobic fermentation processes without producing peculiar smell, and producing wide market value of organic fertilizer and liquid fertilizer by using kitchen waste and municipal sludge waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for preparing biological organic fertilizer using municipal sludge or kitchen closed aerobic biogas residue.'(Drawing includes non-English language text)'
NOVELTY - Method of preparing Chinese pine pollen, involves mixing chromium salt, disodium selenate and organic fertilizer at 26-35 degrees C and fermenting for 3-5 weeks, mixing chromium salt, disodium selenate and organic liquid fertilizer, completely stirring at 26-35 degrees C and fermenting for 2-4 weeks to obtain rich microorganic liquid, adding organic liquid and water, and uniformly spraying on pine pollen such that organic microelement content is improved by more than 10 times.    USE - The method is useful for preparing Chinese pine pollen used for treating diabetes (claimed).    ADVANTAGE - The content of organic trace element in the pine pollen is improved by more than 10 times.
NOVELTY - This utility model claims one kind of organic waste producing organic fertilizer system, comprising a stage processing system, processing main body and organic fertilizer packaging system, processing system's fermentation tank is connected with the feeding port, processing main body comprises a bacteria tank and fermentation tank, tank and the fermentation tank feeding port's, the clapboard is divided into aerobic reaction zone and anaerobic reaction zone fermentation tank, upper part is provided with an overflow groove, an aerobic reaction region is located in the fermentation tank feeding port's one end, and one end of the discharging port is provided with an aeration stirrer, an anaerobic reaction region's's fermentation tank, fermentation tank's organic fertilizer of the packaging system. Said organic waste organic fertilizer after the system taking organic waste with aerobic fermentation under aerobic reaction zone, in the overflow from the overflow into the anaerobic reaction area and oxygen-free, taking the anaerobic fermentation reaction zone, which not only can make the liquid fertilizer in a short time, and the manufacture's odour generated in the process;
NOVELTY - Preparation of formaldehyde scavenging agent comprises weighing raw materials, mixing, and spray drying to obtain powder. The raw materials comprise 10-80 pts. wt. kernel extract, 10-50 pts. wt. maltodextrin, 5-45 pts. wt. starch, and 5-20 pts. wt. calcium gluconate, where kernel extract is peach extract, apricot extract or jujube extract.    USE - Method for preparing formaldehyde scavenging agent (claimed) used for killing bacteria in decorative material and polymerized board.    ADVANTAGE - The agent has strong bactericidal and antimicrobial ability, does not cause secondary pollution, and has sterilizing ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of peach extract comprising taking dried peach and introducing into dry distilling furnace; carrying out flue gas condensing at 120-400 degrees C; standing and precipitating; and distilling supernatant at 105-130 degrees C.
NOVELTY - An antibacterial formaldehyde scavenger comprises 10-50 pts. wt. hawthorn extract, 10-20 pts. wt. Angelica extract, 5-15 pts. wt. pomegranate extract, 1-5 pts. wt. ylang-ylang essential oil, 1-5 pts. wt. lavender essential oil, 1-5 pts. wt. clove essential oil, 10-20 pts. wt. absolute ethyl alcohol and 30-50 pts. wt. water.    USE - Antibacterial formaldehyde scavenger used for car.    ADVANTAGE - The formaldehyde scavenger does not contain chlorine and harmful chemical substance, improves air quality, purifies air, and is nontoxic and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of hawthorn extract comprising taking dried hawthorn and introducing into dry distilling furnace; carrying out flue gas condensing at 120-400 degrees C; standing and precipitating; and distilling supernatant at 105-130 degrees C.
NOVELTY - Preparation of soil-less tomato culture substrate comprises drying and roasting solid material and dairy manure, uniformly mixing to obtain solid substrate, spraying nutrient solution, uniformly mixing and naturally fermenting at 15-30 degrees C for 11-12 days. The nutrient solution is aqueous solution comprising 5-6 g/L sodium nitrate, 3-4 g/L urea, 2-3 g/L copper nitrate, 4-5 g/L manganese nitrate, 45-65 g/L ferrous sulfate, 3-5 g/L ammonium phosphate and 2-3 g/L ammonium citrate.    USE - Method for preparing soil-less tomato culture substrate (claimed).    ADVANTAGE - The low-cost culture substrate reduces dosage of agrochemicals.
NOVELTY - A bag material comprises 0-30 wt.% tobacco stems, 51-81 wt.% sawdust, 18 wt.% wheat bran, 1 wt.% gypsum powder and 60-65 wt.% water.    USE - Bag material used for growing mushroom (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bag material and growing mushroom comprising crushing tobacco stems, adding wheat bran, gypsum powder and water, packaging, sterilizing, inoculating and growing mushroom mycelium.
NOVELTY - The system comprises a water body arranged on one side of water nano-bubble generating device disposed on a water dreg fishing-out device, a self-sucking water pump, a dehydrating device having the water pump with a cylindrical opening tube, and a floating storage mechanism. The nano-bubble generating device is provided with a rear for fermentation and a scum rotating fermentation device. An input end of the self-sucking water pump and the opening tube are tightly connected with an upper tube that is provided with a small hole and coated with at least one layer of filter film.    USE - The system is useful for processing algae scum harmless resource (claimed).    ADVANTAGE - The system is capable of processing algae scum harmless resource in an eco-friendly manner.    DETAILED DESCRIPTION - The system comprises a water body arranged on one side of water nano-bubble generating device disposed on a water dreg fishing-out device, a self-sucking water pump; a dehydrating device having the self-sucking water pump with a cylindrical opening tube, and a floating storage mechanism. The nano-bubble generating device is provided with a rear for fermentation and a scum rotating fermentation device. An input end of the self-sucking water pump and the opening tube are tightly connected with an upper tube that is provided with a small hole and coated with at least one layer of filter film. The tube is arranged on the floating storage mechanism. An outer wall of the tube is corrugated. An output end of the self-sucking water pump output is provided with a deodorizing gas processing mechanism.
NOVELTY - Production of compound organic fertilizer comprises adding 1/10 natural sodium alginate to municipal sludge, semi-flocculating, and dehydrating; adding sawdust, corn straw powder, wheat bran, corn core, and chicken manure, adding 3% phosphoric acid solubility material, 3% heavy metals passivation material and 5% photosynthetic bacteria containing actinomycetes, lactic acid bacteria, microzyme, and Bacillus, fermenting for 5-6 days, turning once, and maintaining temperature at less than 55 degrees C for 3-6 days; and spreading, airing, drying until water content is less than 18% and crushing.    USE - Method for producing compound organic fertilizer (claimed).    ADVANTAGE - The method reduces loss of beneficial bacteria to ensure quality.
NOVELTY - A fertilizer comprises 85-87 wt.% papermaking sludge, secondary sedimentation sludge, and floating sludge, 10-12 wt.% grass bran, 1 wt.% organic fertilizer fermentation agent, 1 wt.% bactericide, 0.5 wt.% amino acid chelate, and 0.5 wt.% humic acid chelate.    USE - Fertilizer.    ADVANTAGE - The fertilizer has economic and social benefits.    DETAILED DESCRIPTION - A fertilizer comprises 85-87 wt.% papermaking sludge, secondary sedimentation sludge, and floating sludge, 10-12 wt.% grass bran, 1 wt.% organic fertilizer fermentation agent, 1 wt.% bactericide, 0.5 wt.% amino acid chelate, and 0.5 wt.% humic acid chelate. The fertilizer is prepared by dehydrating sludge till moisture content is 30%, mixing, and drying; adding organic fertilizer fermenting agent and grass bran, uniformly mixing, where water content is 55-60%, sealing, and fermenting for 25-30 days in summer or fermenting for 65-70 days in winter, where fermentation temperature is 40-60 degrees C; and adding bactericide, amino acid chelate, and humic acid chelate, uniformly mixing, and discharging.
NOVELTY - An organic fertilizer comprises 60-70 wt.% sludge, 27-35 wt.% organic waste, and 3-5 wt.% biomass fermentation enzyme.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer improves soil structure, has low cost, and improves environment.
NOVELTY - Treatment of composite sludge comprises adding auxiliary material into sludge, stirring, and regulating moisture content to 50-60%; adding straw and composite microbial agent, fully stirring, and fermenting; fermenting at more than 55 degrees C for 2 days, fermenting at below 50 degrees C on third and fourth day, turning, uniformly stirring, fermenting at 70 degrees C on fifth day, reducing temperature in seventh to eight day, and turning; and fermenting at 30-40 degrees C on tenth and fourteenth day, stirring every 2-3 days, and fermenting for 21 days total until moisture content is 30%.    USE - Method for treating composite sludge (claimed) used as compost.    ADVANTAGE - The method does not need artificial aeration condition, has simple turning process, low in investment, and avoids loss of nutrient in compost.
NOVELTY - A bio-organic fertilizer is prepared by mixing humus, sawdust, amino acid, algae powder, bone meal, trace elements, cow manure, and licorice powder, fermenting for 3-5 days, adding fulvic acid, stirring for 50-60 minutes, unloading, stacking, composting for 5-7 days, granulating, extruding, drying, cooling, and packing.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method is simple and convenient. The fertilizer is effective and has less odor.
NOVELTY - An organic compound fertilizer comprises 25-30 pts. wt. potassium humate, 20-24 pts. wt. weathered coal, 12-16 pts. wt. peat, 1-2 pts. wt. nanocarbon, 130-135 pts. wt. bean dregs, 2-3 pts. wt. brown sugar, 12-15 pts. wt. bamboo charcoal powder, 15-18 pts. wt. maifan stone, 6-8 pts. wt. zeolite, 17-19 pts. wt. urea, 3-4 pts. wt. sodium selenite, 7-9 pts. wt. ferrous sulfate, 3-4 pts. wt. manganese sulfate, 2-3 pts. wt. zinc sulfate, 13-16 pts. wt. soil conditioner and 1-2 pts. wt. effective microorganism.    USE - Organic compound fertilizer.    ADVANTAGE - The fertilizer improves soil quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic compound fertilizer comprising mixing potassium humate, weathered coal, peat, nanocarbon, bean dregs, brown sugar, bamboo charcoal powder, maifan stone, zeolite and effective microorganism, adding water, piling, fermenting for 10-15 days, adding remaining raw materials, mixing, granulating, and drying.
NOVELTY - Composite organic biological fertilizer comprises 14.5-25.2% humic acid, 33.5-45.1% biochar, 22.5-35.5% chemical fertilizer, and 10.2-15.4% bentonite. For each 1 kg of compound fertilizer, 10-20 ml mixed microbial inoculum is added. The chemical fertilizer comprises urea, calcium hydrophosphate and potassium sulfate at a weight ratio of 40-45:35-45:10-20. The mixed microbial inoculum comprises Bacillus amyloliquefaciens, Bacillus subtilis and Trichoderma at volume ratio of 30-40:35-45:25-35.    USE - Composite organic biological fertilizer used for supplementing organic matter to soil, activating phosphorus and potassium soil fertilizer, improving disease resistance of crops, and preventing and controlling soil borne and crop replant diseases.    ADVANTAGE - The fertilizer is non-toxic and environment-friendly, has high-efficiency, and can be used independently or as a mixture with fertilizer additive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising uniformly mixing microbial inoculum components, uniformly mixing urea, calcium hydrogen phosphate and potassium sulfate; crushing straw, putting in high-temperature cracking furnace, heating to 300-500 degrees C under anaerobic condition to generate biochar, crushing, passing through 200-300 mesh sieve, uniformly stirring humic acid, biochar, chemical fertilizer, and bentonite; spraying fertilizer with mixed microbial inoculum, and uniformly mixing.
NOVELTY - Straw mushroom culturing base material comprises 300-600 pts. wt. bagasse, 100-400 pts. wt. sludge, 0-200 pts. wt. straw, 0-200 pts. wt. corn, 0-10 pts. wt. bran, 5-10 pts. wt. compound fertilizer, 5-10 pts. wt. gypsum, 5-8 pts. wt. lime, and 4-8 pts. wt. urea.    USE - Straw mushroom culturing base material.    ADVANTAGE - The culturing base material lowers straw mushroom production cost, reduces environmental pollution, and has mushroom cultivation biological material conversion rate of up to more than 40%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of straw mushroom culturing base comprising preparing raw materials, spraying 1% lime water spraying, taking pre-wet bagasse, spreading pre-wet bagasse at the lowest layer, spreading other raw material, stacking up layer by layer to a uniform height of 1.5 m, width of 1.2-1.6 m, and length of 2.0-3.0 m; sterilizing culturing material in a room by spraying 0.5% dichlorvos, closing door and window for 24 hours, mixing with formaldehyde and sawdust, closing door and window, fumigating for 2 days; piling for 3-5 days, raising reactor temperature to 65 degrees C for 3-4 days, hot filtering, laying on bed; fermenting culture material, controlling indoor temperature at 68-75 degrees C, keeping for 6-9 hours, taking culture material, post-fermenting, ventilating culture material; inoculating at 35 degrees C; taking mushroom and harvesting.
NOVELTY - Preparing 9-oxonerolidol from camphor plant, comprises drying camphor plant, and crushing into powder; mixing the powder with ethanol in distilled water, extracting 1-3 times, mixing the extracts, filtering, removing insoluble matter and concentrating the filtrate to obtain extract; dissolving camphor powder with distilled water, extracting with petroleum ether solution in distilled water or ethyl acetate or n-butanol, and concentrating under reduced pressure to obtain extract; and gradient eluting, detecting target product by thin layer chromatography, and concentrating into extract.    USE - The method is useful for preparing 9-oxonerolidol from camphor plant (claimed).    ADVANTAGE - The method is easy, economical, green and environmentally-friendly. The product has high purity.    DETAILED DESCRIPTION - Preparing 9-oxonerolidol from camphor plant, comprises (i) drying camphor plant at 30-45 degrees C, and crushing into powder of 10-60 meshes in a traditional Chinese medicine crusher; (ii) mixing the powder with 40-80% ethanol in distilled water in the ratio of 1-2 g :20-80 ml, extracting with stirring at 30-90 degrees C for 1-3 times, each time for 1-7 days, mixing the extracts, filtering, removing insoluble matter and concentrating the filtrate under reduced pressure, to obtain extract; (iii) dissolving camphor powder with 3-10 times of distilled water, extracting with 1/3-2 times of petroleum ether solution in distilled water or ethyl acetate or n-butanol, and concentrating under reduced pressure to obtain extract; and (iv) using 200-400 mesh silica gel as stationary phase, and petroleum ether-ethyl acetate the volume ratio of 8-1:4-1 as solvent system, gradient eluting, detecting target product by thin layer chromatography, and concentrating into extract.
NOVELTY - Tetrahydroindole derivatives (I) are new.    USE - (I) are useful for preparing anticancer drugs (Claimed).    ADVANTAGE - The preparation method: utilizes cheap non-transition metal catalyst, which reduce the production cost; has simple operation, and easily controllable mild reaction condition; is safe and environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Tetrahydroindole derivatives of formula (I) are new.    R1, R3 = H or methyl;    R2 = aryl or heteroaryl; and    R4 = aryl or cycloalkyl.    An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Extracting Hericium erinaceus streptozotocin A, comprises crushing Hericium erinaceus mycelium, performing supercritical carbon dioxide extraction in an extraction kettle and collecting Hericium erinaceus streptozotocin A extract, dissolving in 50-70% ethanol, filtering, adding polyamide resin column to absorb impurities, vacuum extracting and concentrating the extracting solution, crystallizing, refluxing and dissolving the crystal using 80% ethanol, adding activated carbon to decolorize, vacuum extracting, concentrating, crystallizing, and drying.    USE - The method is useful for extracting Hericium erinaceus streptozotocin A (claimed).    ADVANTAGE - The method has low energy consumption and less pollution, and is environmentally friendly.    DETAILED DESCRIPTION - Extracting Hericium erinaceus streptozotocin A, comprises: (a) taking Hericium erinaceus mycelium, crushing into 40-80 meshes, adding in an extraction kettle, using supercritical carbon dioxide extraction, and collecting Hericium erinaceus streptozotocin A extracts, (b) dissolving Hericium erinaceus streptozotocin A extract using 50-70% ethanol, filtering, adding polyamide resin column to absorb impurities, vacuum extracting and concentrating the extracting solution by column and crystallizing, and (c) refluxing and dissolving the crystal using 80% ethanol, adding activated carbon to decolorize, vacuum extracting, concentrating, crystallizing, and drying to obtain Hericium erinaceus streptozotocin A product.
NOVELTY - The utility model claims one integrated kitchen garbage degradation device, comprising a box body, the box body is provided with degradation groove, heating and heat preservation layer, a device cavity, a humidity sensor, a temperature sensor, a deodorizing device, a crushing device, an exhaust pump and stirring device, the stirring device comprises a motor and the motor through chain's stirring shaft, the stirring shaft are staggered up is fixed with a stirring rod, the front side of the box is further provided with a control chamber and automatic garbage conveying device, an automatic garbage transfer device by the motor the kitchen garbage automatic transfer to a crushing device, a garbage crushing the degradable's groove degradation, deodorizing device and exhaust pump is used for purifying and pump's exhaust gas in the device. In time using the kitchen garbage degradation groove's has been added proper amount of degradation strain, it can automatically control temperature's degradation tank maintain a certain's range and automatic stirring, degrading, deodorizing and exhausting, and environment-friendly's more effectively the organic waste into organic fertilizer.
NOVELTY - This utility model claims one kind of organic fertilizer turning processing device, comprising a box body, said box body is provided with a stirring shaft, said upper stirring shaft is equipped with a stirring blade, said stirring shaft is connected with the motor drive is set on the outer wall of the box body, said box body's one side is provided with a feeding port, the upper part is provided with a discharging port, the bottom is provided with a stop mechanism's universal wheel, said feeding port is connected with a spiral conveying machine, it's This utility model has the following advantages: capable of taking movable operation to prevent the material block in the box body, the structure is simple, operation is simple, it is convenient and practical, the working efficiency is high.
NOVELTY - The utility model claims one fertilizer production drying device, comprising a roller, a fixed's track ring and the outer wall of the roller upper ring, said upper ring gear engaged with the drive gear, and an outer wall of said roller is fixed with a shaft's base by hinge shaft is equipped with said shaft base upper hammer in the inner cavity of said roller is provided with a tubular reactor's, said tubular reactor comprises a coaxial and fixedly connected with each other's reaction tube and spraying pipe, said reaction tube and spraying pipe's's inner cavity of said upper reaction pipe is provided with a steam interface and sulphuric acid interface, said steam interface is connected with a steam pipeline, said upper interface is connected with sulphuric acid sulphuric acid pipeline, said upper spraying pipe is provided with a spraying opening, the utility model's advantages can be adhered vibrating, maintain the inner wall's cleaning by sulphuric acid and steam to provide heat energy to save energy consumption's the particle's inner wall of roller; Has simple structure, and it is convenient and practical.
NOVELTY - Esterification of waste oil comprises placing waste oil in storage tank, pumping to heat exchanger, preheating at 50-60 degrees C, heating at 100-110 degrees C, adding 0.1-0.5 wt.% catalyst, refining using methanol with flow rate of 0.7-0.8 m3/hour, reacting at 100-110 degrees C for 2-3 hours, carrying out gasification, cooling, recycling, discharging and collecting.    USE - Method for esterifying waste oil for biodiesel production (claimed).    ADVANTAGE - The method is low-cost and capable to produce with high product yield.
NOVELTY - A water soluble fertilizer comprises balance component A, and 30-50 pts. wt. component B. The component A comprises 12-18 pts. wt. zinc sulfate, 55-75 pts. wt. boric acid, 10-20 pts. wt. magnesium sulfate, 0.3-1 pts. wt. EDTA, 1-2 pts. wt. sugar, 1-5 pts. wt. citric acid, and 3-10 pts. wt. humic acid. The component B is a composite organic matter.    USE - A water soluble fertilizer.    ADVANTAGE - The fertilizer improves yield, quality of crop and soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a water soluble fertilizer comprising mixing raw materials, crushing the mixture, adding water to the crushed mixture at a ratio of 1:0.5-1.5, stirring at a speed of 20-100 revolutions/minute for 4-6 hours, filtering, concentrating, and drying at 80-105 degrees C.
NOVELTY - A benzopyrone is new.    USE - New benzopyrone for quinone synthesis (claimed).    ADVANTAGE - Benzopyrone is low cost, environment-friendly, and has high yield.    DETAILED DESCRIPTION - A benzopyrone of formula (I) is new. INDEPENDENT CLAIMS are included for:    (1) preparation of benzopyrone which involves condensation of benzopyran-1,4-dione-tert.-butylcyclohexyl acetaldehyde in the presence of amine reagent; and    (2) application of benzopyrone in quinone synthesis.    DESCRIPTION OF DRAWING(S) - The drawing shows a NMR spectra of synthesized quinone.
NOVELTY - An imidacloprid detecting method involves preparing graphene oxide modified glassy carbon electrode by diluting graphene oxide with distilled water and dispersing to obtain oxidized graphene dispersion liquid, and coating graphene oxide dispersed droplets in a clean glassy carbon electrode surface, and volatilizing to obtain electrode. The graphene oxide glassy carbon electrode is placed in a modified buffer solution, and nitrogen is introduced followed by adding imidacloprid, using cyclic voltammetry, detecting the electrode electrochemical response of imidacloprid.    USE - Method for detecting imidacloprid in onion, tomato, cucumber, celery, and rape vegetable groups, and for food testing.    ADVANTAGE - The method enables detecting imidacloprid with good electro-catalytic performance, fast current response, high sensitivity, low detection limit, good reproducibility and stability characteristics, and low production cost, ease of operation, selectivity strong, environmentally friendly and non-toxic to humans.    DETAILED DESCRIPTION - An imidacloprid detecting method involves preparing graphene oxide modified glassy carbon electrode by diluting graphene oxide with distilled water to dilute and ultrasonically dispersing to obtain oxidized graphene dispersion liquid, and coating graphene oxide dispersed droplets in a clean glassy carbon electrode surface, volatilizing the clean glassy carbon electrode surface coated with solvent to obtain graphene oxide modified glassy carbon electrode. The graphene oxide glassy carbon electrode is placed in a modified buffer solution, at pH of 2.8-7.5, and nitrogen is introduced for 5-20 minutes, followed by adding imidacloprid, using cyclic voltammetry with scanning rate of 100-200 mV/second, detecting the graphene oxide modified glassy carbon electrode electrochemical response of imidacloprid.
NOVELTY - Laninamivir octanoate is prepared by mixing zanamivir and methanol, adding acid cation resin for reaction to obtain zanamivir methyl, reacting with dimethyl carbonate under alkaline condition, reacting with methyl iodide under alkaline condition, reacting with alkaline solution, adjusting pH to neutral with acid cation resin, and reacting with capryloyl chloride.    USE - Preparation of laninamivir octanoate (claimed).    ADVANTAGE - The process is simple, low cost with low energy consumption, and environment-friendly, and has nontoxic and non-explosive reagents, and the product has high purity.    DETAILED DESCRIPTION - Laninamivir octanoate of formula (14) is prepared by mixing zanamivir of formula (15) and methanol, adding acid cation resin for reaction to obtain zanamivir methyl of formula (16), reacting with dimethyl carbonate under alkaline condition to obtain compound of formula (17), reacting with methyl iodide under alkaline condition to obtain compound of formula (18), reacting with alkaline solution, adjusting pH to neutral with acid cation resin to obtain compound of formula (19), and reacting with capryloyl chloride.    DESCRIPTION OF DRAWING(S) - The drawing shows a reaction equation of preparation of laninamivir octanoate.
NOVELTY - A kind of sewage treatment easy to replace a filling device, comprising a filling device and filling device, a filling device is made of fibre beam are uniformly fixed to combine with the pattern on the plastic ring, a filler and a hollow plastic tube, a rope according to the order from a connected in series, the upper end is fixed on upper-layer reinforcing steel bar bracket, the lower end is fixed on the spherical filler. This utility model is convenient to operate, it saves material, it is convenient for the microorganism sampling experiment research on the fibre and daily operation and maintenance.
NOVELTY - Fertilizer prepared by drying agriculture and forestry waste, crushing to obtain powder, carrying out pyrolysis reaction at 300-700 degrees C for 1-5 hours, cooling to room temperature, grinding, sieving, adding bacterial liquid with a concentration of 106-108 colony forming unit (cfu)/ml, microbial inoculum and bio-char, fermenting for 10-24 hours, separating solid from liquid to obtain bio-carbon in a weight ratio of 1:1-6, adding 4 wt.% of binder, and uniformly mixing, is claimed.    USE - The fertilizer is useful for farmland (claimed).    ADVANTAGE - The fertilizer is simply prepared with reduced organic contamination in a simple, low cost and environment friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of fertilizer for farmland comprising adding in farmland soil of 20 cm of surface layer of 100-1000 kg/hectare, and turning soil on second level.
NOVELTY - Planting material comprises 25-35 wt.% of chestnut tree meal , 18-22 wt.% of corn meal, 9-15 wt.% of oak chip, 18 wt.% of corncob, 15 wt.% of wheat bran, 2 wt.% of corn flour, 1 wt.% of gypsum powder and 2 wt.% of lime powder.    USE - Used as planting material.    ADVANTAGE - The planting material is cost-effective, and has good ventilation property, preserving property and biological efficiency of 117.2-125.8%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the planting material comprising drying the raw materials to exposure for 1-2 days, killing the raw materials using UV light, pre-wetting and mixing the red mushroom, chestnut tree meal, corn meal and oak chip under a dry state condition and uniformly stirring, carrying out pre-wet with 2% of lime water solution and then stacking and fermenting the wet material with a piling height of 1-1.2 m and width of 2-3 m, cultivating 300-500 kg of the stacked material with a diameter of 10-15 cm, turning the cultivated material at 60 degrees C for 24 hours and adding with corn core, bran, corn powder, gypsum powder and auxiliary material, adding the stack material with water and turning for 4-5 times and fermenting for 6-7 days until the water content is 63-65%, bagging the fermented material into a polypropylene plastic bag, inserting the material into the plastic bolt and then sterilizing and cooling into a pot at 100 degrees C for 8-10 hours, and naturally cooling the sterilized material to 25 degrees C.
NOVELTY - Preparing axitinib comprises using 6-halo-1H-indole as raw material, carrying out oxidative rearrangement reaction to obtain 6-halo-3-formyl-1H-indazole, reacting 6-halo-3-formyl-1H-indazole and N-methyl-2-mercapto-benzamide to obtain N-methyl-2-((3-formyl-1H-indazol-6-yl) thio) benzamide, adding ylide reagent and carrying out Wittig reaction to obtain axitinib.    USE - The method is useful for preparing axitinib (claimed).    ADVANTAGE - The method has simple preparation technique, is economical and environmentally friendly, and is suitable for industrial production.
NOVELTY - Denitrifying salt containing sewage comprises adding microbial inoculum into a sewage treatment system and then heating at of 18-40 degrees C and pH value of 7-9 and dissolving, and adding nitrogen to carry out nitrification and denitrification treatment process, where the microbial inoculum comprises Staphylococcus cohnii, Arthrobacter creatinolyticus, Paracoccusdeni trificans and Methylobacterium phyllospherae according to preservation number of CGMCC NO: 3657, CGMCC NO: 3658, CGMCC NO: 3659, CGMCC NO: 3660.    USE - The method is useful for denitrifying salt containing sewage (claimed).    ADVANTAGE - The method denitrifies the salt containing sewage with improved absorbing performance, good water quality and impact resistance.
NOVELTY - Underwater marsh gas collecting device comprises a biogas bonnet (1), an air flow controller (2), a gas collecting bonnet (3), a high pressure pipe (4), a high pressure water flow nozzle (5), a propeller, a safety valve, pressure gauge, a booster pump, a control table, a water-gas separator, a desulfurizer, a gas pipe and an air storage tank.    USE - Used as an underwater marsh gas collecting device.    ADVANTAGE - The device: has compact structure, low cost and strong adaptability; and is good for relieving energy crisis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for collecting underwater marsh gas using the underwater marsh gas collecting device, comprising (i) firstly discharging the air from the gas collecting bonnet, opening the booster pump, flowing the high pressure water flow through the high pressure water flow nozzle from the bottom water sludge, covering the t bottom of the water body, and overflowing in the form of marsh gas bubbles; (ii) when the marsh gas in the gas collecting bonnet reaches certain amount, opening the 12 single-way valves installed on the air flow controller, and then conveying into the biogas bonnet; (iii) manually or automatically open the safety valve through the water-gas separator for separating water and gas; carrying out desulfurization in the desulfurizer, finally entering into the gas storage tank through the gas pipe, and completing collecting; and (iv) repeating the steps (i)-(iii), and continuously collection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the underwater marsh gas collecting device.    Biogas bonnet (1)    Air flow controller (2)    Gas collecting bonnet (3)    High pressure pipe (4)    High pressure water flow nozzle (5)
NOVELTY - This utility model belongs to the field of solid waste treatment field, especially relates to a kind of kitchen garbage, excrement, sludge anaerobic engineering a reactor. Reactor upper part of the outer wall of the tank body in turn from up to down is provided with four annular pipelines, which are respectively with the sludge feeding port, a waste port, outlet, kitchen garbage feeding opening connected with the two groups of stirring device is suspended is fixed is provided with a biogas outlet in the top of the reactor tank body, the top part of the reactor tank body is connected with the marsh gas collecting device, the bottom outlet is provided with checking port, is provided with a circle of scum, floating oil collecting groove, floating slag on the upper part of the annular tube, the floating scum, floating oil collecting groove is connected with the reactor tank body is uniformly distributed with several heating device. The reactor can realize the kitchen garbage, excrement, sludge of a mixed by fermenting in enzymatic reaction, and can be collected and properly discharge floating slag and floating and convenient tank of the rest material for subsequent secondary digestion or other uses.
NOVELTY - A kind of kitchen waste processing anaerobic reactor discharging device, wherein inner part of the anaerobic reactor is provided with a vertical discharging pipe, the top end of the vertical discharging pipe is connected with a reducer union, a reducing joint is connected with elbow, a horizontal discharging pipe, the central line of the transverse discharging pipe is flush with the highest liquid level anaerobic reactor, side transverse discharging pipe passes through the anaerobic reactor and connected with a bent pipe, the first pipe is connected with the discharging pipe, the vertical discharging pipe, from bottom to top is uniformly provided with 2 to 5, through angle steel clamp is connected with the bracket, the bottom bracket is connected with a support leg plate, a bracket foot plate a plane expansion bolt anchored anaerobic reactor. This utility model has simple structure, the structure of the discharging device of kitchen waste anaerobic reactor discharge is smooth and increase the restaurant-kitchen garbage anaerobic stability of marsh gas engineering. The anaerobic reactor discharge device can be widely used for producing marsh gas in the field of kitchen garbage, it has popularization value.
NOVELTY - The method comprises collecting domestic sewage from rural villages at high slope to lower emissions and then discharging into a sewage collection tank along a bottom part of a wastewater infiltration purification system, arranging a wastewater infiltration purification system, a multi-stage purification system and infiltration wetlands to form a ramp ladder and terrace structure with three four levels, filling percolating water and forming a topsoil layer on each level, placing wetland plants on the soil in each level and discharging the sewage water through wetland plants.    USE - The method is useful for purifying rural sewage (claimed).    ADVANTAGE - The method purifies the rural sewage in a simple, cost effective and eco-friendly manner.    DETAILED DESCRIPTION - The method comprises collecting domestic sewage from rural villages at high slope to lower emissions and then discharging into a sewage collection tank along a bottom part of a wastewater infiltration purification system, arranging a wastewater infiltration purification system, a multi-stage purification system and infiltration wetlands to form a ramp ladder and terrace structure with three four levels, filling percolating water and forming a topsoil layer on each level of the terrace structure, placing wetland plants on the soil in each level, discharging the sewage water from the sewage collection tank from top level of the wetland water percolation system and then passing through wetland plants and water infiltration and percolation bio-absorbable layer in the each level to carry out stepwise purification. An INDEPENDENT CLAIM is included for a stepwise rural sewage filtering and purifying device.
NOVELTY - Producing biogas comprises (1) pretreating the kitchen rubbish, (2) pretreating the traditional Chinese medicine waste residue, (3) adjusting the carbon nitrogen ratio of the pretreated traditional Chinese medicine waste residue and the kitchen rubbish and (4) fermenting the obtained product.    USE - The method is useful for producing biogas (claimed).    ADVANTAGE - The method rapidly produces the biogas with high resource utilization waste in an efficient and eco-friendly manner.
NOVELTY - A kind of pond water purifying device, comprising a support, a purifying pond, a, the fish pond is provided with the to be purified, and the height of the support is greater than the water level height of the pond, a purifying pond is fixed on the support, a purifying pond and are relatively fixed, the water pumping device is set on the lower part of the purifying pool and extends the water of fish pond to be purified, the water outlet of the pumping device is set on the upper part of the purifying pond. A purifying pond is provided with the opening of the containing part, the purification plant, part of the side wall is provided with a drain hole and a drain hole close to the bottom of the containing part, the containing part from bottom to top in turn is provided with gravel base layer, active sludge layer, purifying plant planted in the active sludge layer and extends out from the opening of the containing part.
NOVELTY - A kind of straw milling process to produce device, and device for fermentation after the straw for ball milling process. It is provided with baffle plate in the device, one side of the clapboard is on the upper part of the pre-processing device, a pre-processing device is a feeding port, a lower inner part is ball mill processing device, ball milling device is ceramic grinding device, device component is a discharging port, the other side is fermentation device, the inner part is a stirring device, the stirring device is on the rotating shaft device is connected with the lower end of the rotating shaft is set with a stirring paddle, the middle part is set with separating plate, rotating shaft of the stirring device passes through the separating plate. The time for fermentation of straw enter into pre-treating device by ball milling treatment for ball milling treatment, and carrying out pre-processing step, the stirring device can stir for fermentation, fermentation is separating plate at the lower part to prevent fermenting steam exploded wood fibre straw is not completely, improving the fermenting steam exploded wood fibre straw.
NOVELTY - A kind of horizontal marsh gas fermentation device, comprising a fermentation tank body, a heating system and a stirring mechanism in the fermentation tank body is provided with a feeding port, a discharging port and a slag discharging port, a heating system is set in the fermentation tank in the body, wherein the stirring mechanism comprises a horizontally arranged stirring shaft and a stirring shaft driving mechanism, the two ends of the stirring shaft are respectively provided with support in the fermentation tank body, the stirring shaft driving mechanism is connected with a stirring shaft, the stirring shaft is provided with a plurality of stirring paddle, the included angle of the bottom of the horizontal direction of the fermentation tank body is -15 degrees to 15 degrees. This utility model is low energy consumption stirring, stirring efficiency is high, easy scale amplification, simple and convenient maintenance, wide application range, low construction and operation cost, especially suitable for direct marsh gas fermentation treating dry material mass fraction of 10% to 20% of high-concentration organic waste with high viscosity.
NOVELTY - A kind of grinding pre-processing fermentation device, and device for fermentation after the straw grinding. It is provided with baffle plate in the device, one side of the clapboard is on the upper part of the pre-processing device, a pre-processing device is a feeding port, the feeding port is installed the lower part of grinding device, wherein a device part is a discharging port, the other side is fermentation device, the inner part is a stirring device, the stirring device is on the rotating shaft device is connected with the lower end of the rotating shaft is set with a stirring paddle, the middle part is set with separating plate, rotating shaft of the stirring device passes through the separating plate. The time for fermentation of straw grinding into powder by grinding device enter into pre-processing device, and carrying out pre-processing step, the stirring device can stir for fermentation, fermentation is separating plate at the lower part to prevent fermenting steam exploded wood fibre straw is not completely, improving the fermenting steam exploded wood fibre straw.
NOVELTY - Operating a biogas plant, comprises dewatering the resulting raw digestate, drying to obtain a liquid evaporation concentrate, and back-mixing the liquid evaporation concentrate to the crude fermentation residue.    USE - The method is useful for operating a biogas plant.    ADVANTAGE - The method: utilizes less amount of water and heat; and reduces the quantity of fermentation residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing the above mentioned method.
NOVELTY - It is a method to upgrade biomass for producing solid fuels. After biomass undergoes pulverizing, sieving and drying, it is placed in a reactor and mixed uniformly with dilute acid solution. Then the reactor is placed in a microwave heater and heated by microwaves. Once the temperature in the reactor reaches the set temperature, the biomass is upgraded in a given duration through wet torrefaction. Biomass can be lignocelluloses or agricultural wastes. The properties of biomass and heating value of the biomass can be improved from the wet torrefaction, thereby upgrading the biomass as the alternative fuel of fossil fuels.
NOVELTY - This utility model claims one kind of biomass gasification hot water boiler device, gas conveying pipe is connected to the biomass gasification furnace and gas purifier, gas inlet pipe's one head is connected to the upper gas delivery pipe. The inner wall is connected with a furnace body's in the solid plate, solid plate's central part is fixedly provided with air collecting cover, a gas burner hot air collecting cover is set opposite to the lower end of the furnace body, the lower end's gas burner is equipped with air inlet pipe and gas inlet pipe. Heating tube's head is connected with the top end of one's hot air collecting cover, and the other one head's heating pipe diffusing pipe waste gas, waste gas diffusing out the top end's. The furnace body upper end's outer upper wall is installed with a water inlet pipe and water level balancing pipe close to the fixing plate with a water outlet pipe is installed on the upper body. This hot water boiler device can reduce energy cost, it will not cause too much pollution to the atmosphere, which can improve the hot efficiency and has practical value.
NOVELTY - Processing dead pig compost, comprises paving ground sawdust compost on upper part of a bin having thickness of 30 cm, then stacking dead pig, covering an upper part of dead pig stack with the sawdust to thickness of 20-30 cm, covering other part of the dead pig stack with the saw wooden chip until the naked eyes cannot see dead pig stack, maintaining humidity to 40-60% and temperature to 50-65 degrees C, fermenting the compost for 6 months, and spraying water on surface of the compost for every 10 days, where space between the dead pig to wall is 25 cm, and sawdust contains 20% of water content.    USE - The method is useful for processing dead pig compost (claimed).    ADVANTAGE - The method processes dead pig compost in a simple, cost-effective and eco-friendly manner.
NOVELTY - Organic liquid fertilizer, comprises 20-50 pts. wt. of amino acid, 30-50 pts. wt. of syrup, 30-60 pts. wt. of cotton seed hull, 20-50 pts. wt. of corn cob, 2-10 pts. wt. of microbial agent, 20-200 pts. wt. of high oxygen water.    USE - The organic liquid fertilizer is useful for pomegranate tree (claimed).    ADVANTAGE - The eco-friendly organic liquid fertilizer provides rapid nutrition absorbtion and oxygen absorbtion, and improved cell viability to pomegranate tree.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing organic liquid fertilizer, comprising crushing cotton seed hull and corn cob to obtain a powder with a particle size of 200-300 meshes, then adding into a fermentation tank, adding syrup and high oxygen water, adjusting the pH value of the tank to 6-7, sealing the tank, uniformly stirring at a temperature of 30-35 degrees C and a speed of 20-300 revolutions per minute (rpm), fermenting for 3-10 days, adding amino acid and then stirring for 2-3 days, uniformly sterilizing the mixed liquid, heating the liquid at 25 degrees C and adding microbial agent.
NOVELTY - Inorganic compound fertilizer comprises 34-38 pts. wt. of urea, 56-59 of bicarbonate, 23-26 pts. wt. of potassium chloride, 4-5 pts. wt. of sodium selenite, 2-3 pts. wt. of sodium nitrate, 3-4 pts. wt. of polyacrylamide, 4-5 pts. wt. of alum powder, 3-4 pts. wt. of zinc sulfate, 2-3 pts. wt. of borax and 6-9 pts. wt. of soil conditioning agent.    USE - The inorganic compound fertilizer is useful for improving crop quality.    ADVANTAGE - The inorganic compound fertilizer effectively improves organic matter and fertility in land and soil.    DETAILED DESCRIPTION - Inorganic compound fertilizer comprises 34-38 pts. wt. of urea, 56-59 of bicarbonate, 23-26 pts. wt. of potassium chloride, 4-5 pts. wt. of sodium selenite, 2-3 pts. wt. of sodium nitrate, 3-4 pts. wt. of polyacrylamide, 4-5 pts. wt. of alum powder, 3-4 pts. wt. of zinc sulfate, 2-3 pts. wt. of borax and 6-9 pts. wt. of soil conditioning agent. The soil conditioning agent comprises 12-15 pts. wt. of vermiculite powder, 20-25 pts. wt. of attapulgite, 1-3 pts. wt. of zinc sulfate, 1-2 pts. wt. of sodium selenite, 2-3 pts. wt. of manganese sulfate, 4-5 pts. wt. of magnesium sulfate, 0.4-0.5 pts. wt. of nano carbon, 10-12 pts. wt. of clay, 2-3 pts. wt. of slaked lime, 3-4 pts. wt. of wintergreen oil, 2-3 pts. wt. of boric acid, 4-5 pts. wt. of trimeric sodium phosphate, 1-2 pts. wt. of silane coupling agent KH550-1, 1-2 pts. wt. of corundum powder, 4-5 calcium carbonate powder and balance of water, and is prepared by adding and mixing zinc sulfate, sodium selenite, manganese sulfate, magnesium sulfate and nanocarbon, evenly adding wintergreen oil and then uniformly stirring, adding silane coupling agent, calcium carbonate powder, uniformly mixing, adding silane coupling agent and mixing, granulating the mixture, and drying.
NOVELTY - Welding gas comprises a mixture of gas and additive. The additive comprises a mixture of 1-2 pts. wt. 2-hexanone, 2-4 pts. wt. limonene, 1-2 pts. wt. dimethylbenzene, 3-5 pts. wt. acetone, 0.1-0.2 pts. wt. ferrocene, 2-3 pts. wt. trimethyl phosphate, 1-2 pts. wt. methylcyclopentadienyl manganese tricarbonyl, 2-3 pts. wt. ethylene glycol monobutyl ether, 0.1-1 pts. wt. aluminum isopropoxide, and 0.01-0.02 pts. wt. nanocarbon.    USE - Used as a welding gas.    ADVANTAGE - The welding gas is environmentally friendly and highly efficient (claimed); is harmless to the environment and the operator; generates maximum flame temperature; achieves flame welding and cutting properties; and is suitable for explosive correction operation.
NOVELTY - The machine has a machine frame (4) that is respectively provided with group of driven wheel (17) and group of driving wheel (1). One group of the running electric motor (3) through the main shaft is connected with the driving wheel. The driven wheel is fixed on the fixed base (16). A supporting shaft is fixed on the supporting shaft bearing base (15). A supporting device is fixed on the bearing base (14). A lifting controller (8) is provided to control the lifting motor to drive the electro-hydraulic push rod (9) and steel wire rope (7).    USE - Self-walking type compost turning machine.    ADVANTAGE - The turning efficiency of the machine can be improved. The fermentation period can be shortened significantly. The composting quality can be improved. The adaptability and flexibility of the machine can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the self-walking type compost turning machine.    Driving wheel (1)    Electric motor (3)    Machine frame (4)    Steel wire rope (7)    Lifting controller (8)    Electro-hydraulic push rod (9)    Bearing base (14)    Supporting shaft bearing base (15)    Fixed base (16)    Driven wheel (17)
NOVELTY - Cultivation material, comprises 8-12 wt.% Pecan powder, 10-16 wt.% shell crumbs, 35-45 wt.% nutshell debris, 20 wt.% mushroom residue, 15 wt.% rice bran, 1 wt.% super phosphate, and 1 wt.% calcium carbonate.    USE - The cultivation material is useful for cultivating oyster mushroom (claimed).    ADVANTAGE - The cultivation material produces high yield with good quality, and has biological efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) preparation of the cultivation material, which involves (a) drying above-mentioned raw materials by exposing under UV for 1-2 days to kill bacteria, (b) mixing processed Pecan powder, shell crumbs, and nutshell debris, pre-wetting mixture using water, (c) stacking 300-500 kg mixture to 1-1.2 m height and 2-3 m width for 4 weeks, forming holes in the stacked mixture to 10-15 cm diameter, where stomatal density is 1 a/m3, and allowing the mixture for natural fermentation, (d) maintaining temperature of the mixture at 60 degrees C for 24 hours, turning the mixture once a day, adding remainder raw materials to the mixture, depending on moisture content of the mixture adding water, turning the mixture for 4-5 times in 6-7 days, fermenting the mixture, until moisture content of the mixture reaches 63-65%, (e) bagging the prepared mixture in 17 cmx 35 cmx 0.005 cm polypropylene bags, where each bag contains 1100-1200 g wet material, and (f) sterilizing the mixture at 100 degrees C under atmospheric pressure for 10-12 hours, and cooling the mixture to 25 degrees C or less; and (2) cultivating oyster mushrooms, involves culturing oyster mushroom seeds in prepared bag in dark room at 22-24 degrees C for 24-26 days, where humidity of the mixture is 60-75%, and obtaining mycelium.
NOVELTY - Preparing fertilizer comprises (a) culturing each of the bacteria strains in fermentation broth, and obtaining each of the species; and (b) mixing the bacteria and other components to obtain the fertilizer according to the following ratio: 10-20 parts polyacrylamide, 3-5 parts matrine, 3-5 parts ascorbic acid, 3-5 parts EDTA, 35 parts zinc chloride (ZnCl2), 50-150 copies bacteria, and the rest is water; where the bacteria comprise Bacillus licheniformis, Bacillus subtilis, Streptomyces, and Bacillus laterosporus.    USE - The method is used for preparing fertilizer (claimed).    ADVANTAGE - The method provides fertilizer which can effectively keep the bacteria active, has strong synergy between bacteria, and high efficiency.
NOVELTY - Biological organic fertilizer comprises raw materials comprising 50-60 pts. wt. humus, 15-20 pts. wt. sawdust, 2-5 pts. wt. amino acid, 1-2 pts. wt. potassium humate, 5-8 pts. wt. seaweed, 2-5 pts. wt. bone powder, 2-5 pts. wt. microbial agent, 1-2 pts. wt. microelements, 40-50 pts. wt. dry dairy manure and 2-5 pts. wt. licorice.    USE - As biological organic fertilizer.    ADVANTAGE - The organic fertilizer is convenient to use, cost-effective and environmentally-friendly, has simple structure, balanced nutrition needed by the growth of crop nutrient content, no chemical and long-lasting effect, improves soil effect, and reduces waste.
NOVELTY - Preparing cetirizine hydrochloride intermediate 4-(4-chlorodiphenylmethyl)piperazine-ethanol comprises using 4-chlorodiphenylmethane chloride and hydroxyethyl piperazine as raw material, adding acid-binding agent in an organic solvent in presence of a catalyst, and carrying out one step reaction at 40-60 degrees C to obtain intermediate 4-(4-chlorodiphenylmethyl)piperazine-ethanol, where the mol ratio of 4-chlorodiphenylmethane chloride and hydroxyethyl piperazine is 1:1.3-4, the catalyst is sodium iodide, and the acid-binding agent is potassium carbonate or triethylamine.    USE - The method is useful for preparing cetirizine hydrochloride intermediate 4-(4-chlorodiphenylmethyl)piperazine-ethanol (claimed).    ADVANTAGE - The method: is simple; utilizes economical raw materials; has mild reaction condition and short reaction period; avoids utilization of highly poisonous chloroethanol, thus it is environmentally friendly; and is suitable for large scale industrial production.
NOVELTY - Preparing sludge coal water slurry comprises (i) mixing municipal sludge and a sludge modifier to obtain a mixture, adding the mixture into water to obtain mixed solution, where the amount of the mixed liquid is 2 times of the mixture; (ii) adding the mixed solution into a fluid shock wave processor for carrying out high-pressure treatment to obtain modified sludge; and (iii) crushing raw coal to obtain pulverized coal with particle size of less than 3 mm, conveying the pulverized coal and the modified sludge to a mill, and adding a dispersant, and grinding to obtain sludge coal water slurry.    USE - The method is useful for preparing sludge coal water slurry (claimed).    ADVANTAGE - The method: utilizes alkaline paper-making black liquor and fully utilizes alkaline substances in the black liquor, which saves the chemical raw material modifier; utilizes black liquor of lignin as water coal slurry additive, which may partially or completely replace the water coal slurry additive; and reduces the cost of pulping additives.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the sludge coal water slurry prepared by the above mentioned method.
NOVELTY - An Amylomyces rouxii CZ1 strain deposited under CGMCC NO. 6874, is new.    USE - The strain is useful for preparing biological agent (claimed) used for killing pathogens and parasites in animal and used as fertilizer.    ADVANTAGE - The biological agent can maintain a temperature of more than 50 degrees C for 15 days, can shorten the fermentation period, and can effectively kill pathogens and parasites in animal. After composting fermentation, the compost product nutrient content is high, and can be used as good plant organic fertilizer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a biological agent comprising the strain; and (2) a method for preparing the biological agent comprising culturing Amylomyces rouxii CZ1 strain in liquid fermentation culture medium, and obtaining the fermentation liquid.
NOVELTY - Composite microbial inoculum comprises Phanerochaete chrysosporium fungus, Streptomyces, Bacillus subtilis, Bacillus licheniformis and Bacillus amyloliquefaciens.    USE - The composite microbial inoculum is useful for cow manure, preferably for reducing lignin content in compost (claimed).    ADVANTAGE - The strains can produce rapid warming of manure compost at a high temperature to kill harmful organisms. The inoculum significantly reduces unpleasant odors, and solves environmental pollution. It can rapidly be used in manure fermentation process, and can quickly and efficiently break down organic manure in lignocellulosic substances, thus speeding up the rate of decomposition of compost materials, and can improve product quality of compost for production of bio-organic fertilizer, thus reducing the cost of agricultural production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for preparing composite microbial inoculum comprising: (1) slant culturing: inoculating the microorganism above at 28-30 degrees C for 3-5 days, filtering the ash for 5-7 days, and strain activation; (2) one-grade seed culturing; (3) second grade seed cultivation; (4) strain solid fermentation culturing; and (5) microbial inoculation.
NOVELTY - The device has a electrochemical oxygen probe, a main control board, a loudspeaker, an alarm lamp, an LCD screen, an infrared remote controller, an SD card, a RS485 communication interface, a nickel-hydrogen battery and an external power supply that are connected with each other. The main control board is provided with an ARM (RTM: 32-bit micro-processor), a signal conditioning circuit, a key circuit and a program downloading interface. A power supply control plate is provided with an external power supply interface and a nickel-hydrogen battery interface.    USE - Real-time multi-parameter non-dispersive infrared methane and carbon dioxide concentration testing device for a mine emergency rescue system.    ADVANTAGE - The device can monitor main gas concentration, and has high detection accuracy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a real-time multi-parameter non-dispersive infrared methane and carbon dioxide concentration testing device.'(Drawing includes non-English language text)'
NOVELTY - A one ammonium phosphate in the production slurry's concentrating device, relating to phosphate fertilizer industry and energy-saving technical field of environmental protection, comprising a flash chamber and the concentrating and circulating pump, slurry heater and flash chamber, a condensing water tank and a steam generator, wherein the utility model's is provided with a steam compressor, steam inlet and neutralizing flash's steam compressor, condensing's flash steam outlet, a steam compressor's steam outlet and steam generator's steam through steam inlet steam header pipe is connected with the slurry's heater. The utility model and the flash chamber and concentrated to generate's flash steam enters the steam compressor with the steam generator to generate's fresh steam mixing and has fresh steam consumption, energy-saving and environment-friendly, without cooling circulating water system and so on.
NOVELTY - The utility model claims one kind of semi-automatic small agricultural waste seedling matrix fermentation device, a semi-automatic small agricultural waste substrate applied to grow seedling fermentation device comprises a barrel cover, a vent hole, the inner wall of the heating wire, the heating wire, the hot benzene, a barrel body, a reactor, filtering cotton bracket, a humidifying space, a water pump, a water pipe, a humidifying spray humidifying, humidifying, temperature and humidity controller, a temperature and humidity probe, a micro-humidifying, the air compression pump, small water tank, the utility model uses the livestock manure and crop straw, and carbon nitrogen ratio's arranged in semi-fermenting device taking fermentation and lower screening different agricultural waste the best ratio can replace the resource of grass peat's substrate applied to grow seedling so as to reduce or replace the grass and so on can be regenerated into's resource, reduces cost, and realize the recycling vegetable seedling's agricultural waste. In addition, the utility model has simple structure, convenient operation, and has good's practical application value.
NOVELTY - The fuel cell component (10) comprises a plate (12,14) having multiple channels (32,34,36,38), where a channel is configured differently than other channels such that the channel provides a cooling capacity to a selected portion of the plate and another channel provides lesser cooling capacity to other portion of the plate. The former channel has a cross-sectional area that is generally perpendicular to a direction of flow. The former channel includes an insulating element situated along a section of the former channel. The insulating element resists heat absorption by coolant.    USE - Fuel cell for generating electricity based upon an electrochemical reaction.    ADVANTAGE - The fuel cell component comprises a plate having multiple channels, where a channel is configured differently than other channels such that the channel provides a cooling capacity to a selected portion of the plate and another channel provides lesser cooling capacity to other portion of the plate, and thus reduces the temperature at the portion of the fuel cell that becomes hotter during fuel cell operation, adequately satisfies the cooling needs in all possible fuel cell configurations, and enhances fuel cell performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for managing a temperature within a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell.    Fuel cell component (10)    Plate (12,14)    Cathode catalyst (20)    Anode catalyst (22)    Channels (32,34,36,38)
NOVELTY - Method for producing ethanol, involves feeding a fermentable lignocellulosic biomass feed obtained by treating a starting lignocellulosic biomass to liberate carbohydrates contained and containing the carbohydrates and associated fermentation inhibiting biomass components produced from starting biomass together with the carbohydrates in the treatment, and continuously fermenting fermentable carbohydrate components of the biomass feed at an elevated temperature using an obligatorily anaerobic thermophilic microorganism which is suspended and not immobilised.    USE - The method is useful for producing ethanol (claimed).    DETAILED DESCRIPTION - Method for producing ethanol, involves feeding a fermentable lignocellulosic biomass feed into a continuous fermentation, where the fermentable lignocellulosic biomass feed is obtained by treating a starting lignocellulosic biomass to liberate carbohydrates contained and containing the carbohydrates and associated fermentation inhibiting biomass components including at least one of hydroxymethylfurfural , 2-furaldehyde and acetic acid produced from the starting biomass together with the carbohydrates in the treatment, and continuously fermenting fermentable carbohydrate components of the biomass feed at an elevated temperature using an obligatorily anaerobic thermophilic microorganism which is suspended and not immobilised, where the ethanol is continuously or continually removed during the fermentation and the feed contains a concentration of the fermentation inhibiting compound hydroxymethylfurfural of at least 0.05 g/l, or contains a concentration of the fermentation inhibiting compound 2-furaldehyde of at least 0.5 g/l, or a concentration of the fermentation inhibiting compound acetic acid of at least 5 g/l.
NOVELTY - The multi-tube burner (300) has a burner portion that provides heat within a high temperature fuel reformer. The fuel reformer is provided to convert the hydrocarbon fuel into hydrogen. The flame generation height of the fuel reformer is different, so as to control the length of flame within the fuel reformer.    USE - Multi-tube burner for fuel reformer of fuel cell system, for reforming hydrocarbon fuel e.g. natural gas.    ADVANTAGE - Since the flame generation is available in various heights, the length of flame in the fuel reformer can be controlled effectively. Since an effector is included within the fuel reformer, the activity of the catalyst to become weak can be controlled through the length of flame modulation. Hence the need to change enlargement or reduction of the plant capacity can be enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the multi-tube burner.    Multi-tube burner (300)    Main portion (301)    Fuel supply unit (320)    Oxygen-containing gas supply unit (330)    Electrode (340)
NOVELTY - The separation tank has a permanent magnet (12) that is completely covered in a stainless steel case, positioned in between two cell plates (11) and connected to an anode shaft (5) with a Z plate in between. The magnet creates an electromagnetic field while direct current (DC) current passes through an electrolyte solution. An S or Z shaped stainless steel propeller (13) is attached to shaft to hold cell plates and magnet. The propeller increases a flow speed of solution, such that reaction to produce hydrogen gas is increased when electrical current passes through solution.    USE - Hydrogen separation tank.    ADVANTAGE - The hydrogen gas produced to flow through can be allowed to the hydrogen pipe and the engine combustion chamber. The electrical current is strengthened without adding another battery.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view illustrating the connection of cell plates, magnet, and Z plate to the shaft.    Lid (2)    Anode shaft (5)    Cell plate (11)    Permanent magnet (12)    S or Z shaped propeller (13)
NOVELTY - A hydrogen gas generating device comprises chamber which is compartmentalized to have 1st subchamber and 2nd subchamber, ionomer membrane (30) which sealably separates 1st subchamber and 2nd subchamber, elongated structures (70) containing semiconductive material extending through ionomer membrane and having a bandgap energy of 0.8-1.9 eV, and catalyst (50) which is disposed on surface of elongated structures in 1st subchamber or is disposed on backside of elongated structures in 2nd subchamber when exposed to light.    USE - Device for generating hydrogen gas (claimed).    ADVANTAGE - Voltage generated is greater than 1.23 V. Device has single-junction microwire array decorated with electrocatalyst and embedded in an ionomer membrane.    DETAILED DESCRIPTION - A hydrogen gas generating device comprises chamber which is compartmentalized to have 1st subchamber and 2nd subchamber, ionomer membrane (30) which sealably separates 1st subchamber and 2nd subchamber, elongated structures (70) containing semiconductive material extending through ionomer membrane and having a bandgap energy of 0.8-1.9 eV, and catalyst (50) which is disposed on surface of elongated structures in 1st subchamber in which catalyst on elongated structure performs reduction of 2 moles of hydrogen ion forming hydrogen gas or oxidation of 3 moles of iodine ion forming triiodine ion, or is disposed on backside of elongated structures in 2nd subchamber when exposed to light. An INDEPENDENT CLAIM is included for a process of generating hydrogen gas which involves contacting the device with hydrogen iodide under illumination.    DESCRIPTION OF DRAWING(S) - The drawings show an explanatory view of the unit cell of a photoelectrochemical (PEC) device.    Membrane (30)    Catalyst (50)    N-emitter layer (60)    Elongated structures (70)
NOVELTY - A modified bacterial strain capable of fermenting both hexose and pentose sugars for production of bioalcohol, where a promoter of pyruvate dehydrogenase operon (PDH) is replaced with a promoter of a gene that is expressed under anaerobic conditions, is new.    USE - For fermenting both hexose and pentose sugars for production of bioalcohol from lignocellulosic biomass, where the hexose sugar is selected from glucose, galactose, allose, altrose, mannose, gulose, idose and talose, and the pentose sugar is selected from xylose, arabinose, ribose, lyxose, ribulose and xylulose, (claimed). The bioalcohol includes ethanol.    ADVANTAGE - The modified bacterial strain produces bioalcohol such as ethanol with high productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) preparation of the modified Escherichia coli strain; 2) fermenting hexose and/or pentose sugars involving utilizing the modified Escherichia coli strain for the production of bioalcohol; and 3) fermenting lignocellulosic biomass comprising hexose and pentose sugars with the modified bacterial strain for the production of bioalcohol under aerobic, microaerobic and/or anaerobic conditions involving hydrolyzing the lignocellulosic biomass comprising hexose and pentose sugars; mixing the modified Escherichia coli strain with hydrolyzed lignocellulosic biomass comprising hexose and pentose sugars; and allowing fermentation of the mixture to be carried out in microaerobic conditions to produce ethanol.
NOVELTY - The water electrolysis apparatus (10) has a disc spring (46) which presses a cathode electric power feeding section (42) toward a solid polymer electrolyte membrane (38). The electrolyte membrane includes an upper electrolyte layer (38a) that is arranged at a cathode electric power feeding section side, and a lower electrolyte layer (38b) that is arranged at an anode electric power feeding section side. The upper electrolyte layer comprised of a hydrocarbon type film is formed with current efficiency higher than the lower electrolyte layer comprised of a fluorine-type film.    USE - Differential pressure type water electrolysis apparatus e.g. high-pressure water electrolyzer of unit cell.    ADVANTAGE - The power efficiency can be improved, while suppressing a damage to the solid polymer electrolyte membrane using a simple and economical structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the unit cell.    Differential pressure type water electrolysis apparatus (10)    Solid polymer electrolyte membrane (38)    Upper electrolyte layer (38a)    Lower electrolyte layer (38b)    Cathode electric power feeding section (42)    Disc spring (46)
NOVELTY - Preparing 2-isopropyl-5-methylcyclohexanol (D, L-menthol), comprises: (a) hydrogenating thymol with hydrogen in the presence of a catalyst and optionally in the presence of a solvent; (b) hydrogenating the 2-propyl-(2)-5-methylcyclohexanone (menthone) isolated from (a) with hydrogen in the presence of a catalyst as supported or unsupported catalysts, optionally in the presence of a solvent to give menthol; (c) separating neomenthol, which is formed alongside with menthol; and (d) optionally carrying out an isomerization reaction of neomenthol to give menthol.    USE - The process is useful for preparing 2-isopropyl-5-methylcyclohexanol (D, L-menthol) (claimed).    ADVANTAGE - The process is capable of simply and energy-efficiently preparing 2-isopropyl-5-methylcyclohexanol with high purity and yield and without forming D,L-isomenthol and undesired by-products.    DETAILED DESCRIPTION - Preparing 2-isopropyl-5-methylcyclohexanol (D, L-menthol), comprises: (a) hydrogenating thymol with hydrogen in the presence of a catalyst consisting of elements of Group VIII B (iron-platinum-group) consisting of platinum, rhodium, ruthenium, and palladium, preferably palladium, and optionally in the presence of a solvent; (b) hydrogenating the 2-propyl-(2)-5-methylcyclohexanone (menthone) isolated from (a) with hydrogen in the presence of a catalyst from a group VIII b (iron-platinum group) consisting of platinum, rhodium, ruthenium and palladium, preferably rhodium as supported or unsupported catalysts, optionally in the presence of a solvent to give menthol; (c) separating neomenthol, which is formed alongside with menthol; and (d) optionally carrying out an isomerization reaction of neomenthol to give menthol, where the steps (a) and/or (c) are carried out at temperatures of 60-200 degrees C and at a pressure of 1.1 bar.
NOVELTY - The vegetable production system has a marsh gas production system that is arranged in a greenhouse (18). A vegetable planting system (14) is arranged in the greenhouse. A module-type biogas production system is arranged on the greenhouse. An insulating chamber (9) is wrapped on a fermentation room (3) formed in the greenhouse.    USE - Vegetable production system used in greenhouse.    ADVANTAGE - The utilization rate of production system can be improved effectively. The working time of labor can be reduced. The production system can be operated conveniently. The production system can be assembled and disassembled easily. The production system can be transported efficiently. The floor area of greenhouse can be reduced. The heat preservation effect of production system can be improved. The production efficiency of production system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the vegetable production system used in greenhouse.    Fermentation room (3)    Heating device (4)    Insulating chamber (9)    Vegetable planting system (14)    Greenhouse (18)
NOVELTY - Dead livestock and poultry are ecologically processed by dividing, sterilizing at greater than or equal to 140 degrees C for greater than or equal to 1 hour, crushing, mixing in beneficial bacteria, wheat bran, sawdust and brown sugar, decomposing using fly maggot, and separating.    USE - Method for ecologically processing dead livestock and poultry for producing active organic fertilizer (claimed).    ADVANTAGE - The process has short physical and chemical operation, zero wastewater, waste residue and pollution production, high yield and good quality. It comprehensively utilizes fly maggots, extends industrial chain, and improves resource utilization.
NOVELTY - The garbage bin has a top cover (5) that is arranged above a lamp case provided with a lead connected to a storage battery (8) and illuminating lamp (7). A supporting beam (10) is filled with the cavity of the thermoelectric conversion material (4). A microorganism storing box (9) is arranged in the upper surface of the top cover. A through-hole is formed in surface of microorganism storing box. A fertilizer collecting bin (13) is arranged at upper bottom plate of garbage collecting chamber which is uniformly distributed with a leaking hole.    USE - Environment-friendly garbage bin.    ADVANTAGE - The garbage can be decomposed into fertilizer for secondary utilization. The garbage bin can be provided with nighttime illumination function, by decomposing the waste heat into electric energy for illuminating lamp.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the environment-friendly garbage bin.    Thermoelectric conversion material (4)    Top cover (5)    Illuminating lamp (7)    Storage battery (8)    Microorganism storing box (9)    Supporting beam (10)    Fertilizer collecting bin (13)
NOVELTY - The device has fermentation cylinder that is set on lower portion of crushing device. The opening end of fermentation cylinder is connected with discharge hole of crushing device (400) corresponding to the closed end of mounting base and upper transmission mechanism. The driving motor is connected with the upper end of stirring auger suspended in middle portion of fermentation cylinder. The lower end of fermentation cylinder is passed through the sealed end to rotate mounting base and another transmission mechanism with drive motor.    USE - Environment-friendly kitchen waste processing device.    ADVANTAGE - The device is featured with high degree of automation, small volume, and energy-saving. The waste processing amount is large, the operation of device is convenient, and the labor intensity is reduced. The kitchen garbage of 150-200 kilograms can be processed in 24 hours, and the water content is not more than 25% of organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the environment-friendly kitchen waste processing device.    Garbage barrel lifting device (100)    Feeding device (200)    Extruding device (300)    Crushing device (400)    Electric control device (600)
NOVELTY - Method for preparing highly compressed fertilizer cake, involves preparing compost using fermented tea leaves, plant straw and animal excrement as raw materials, composting at high temperature (aerobic conditions), adding water retention agent to the compost, and molding and pressing the product (high compression).    USE - The method is useful for preparing highly compressed fertilizer cake (claimed).    ADVANTAGE - The method is convenient to perform, and less labor intensive, and cost-effective, and simple. The fertilizer cake prepared by the method improves quality of crops, promotes growth of crops, and utilizes less water.
NOVELTY - A carfentrazone-ethyl chloropropionic acid (I) is prepared by mixing carfentrazone-ethyl derivative (i), iodine powder, organic solvent, and 10-60% fuming sulfuric acid at 25-55 degrees C for 2-10 hours resulting to iodine-containing carfentrazone-ethyl derivative (ii), adding ethyl acrylate, palladium catalyst and alkali under nitrogen atmosphere, and heating with acetonitrile or N,N'-dimethylformamide at 90-145 degrees C for 2-48 hours.    USE - Method for preparing carfentrazone-ethyl chloropropionic acid (claimed).    ADVANTAGE - The method is easy, safe, and environment-friendly. It has low cost.    DETAILED DESCRIPTION - A carfentrazone-ethyl chloropropionic acid of formula (I) is prepared by mixing carfentrazone-ethyl derivative of formula (i), iodine powder, organic solvent, and 10-60% fuming sulfuric acid at 25-55 degrees C for 2-10 hours resulting to iodine-containing carfentrazone-ethyl derivative of formula (ii), adding ethyl acrylate, palladium catalyst and alkali under nitrogen atmosphere, heating with acetonitrile or N,N'-dimethylformamide at 90-145 degrees C for 2-48 hours resulting to ethyl crotonate-containing carfentrazone-ethyl derivative of formula (iii), adding potassium monopersulfate composite salt with concentrated hydrochloric acid at 25-40 degrees C for 24-72 hours, adding triethylamine with 1:36 mole ratio at room temperature for 0.2-5 hours, adding dichloromethane and saturated sodium chloride, drying via anhydrous magnesium sulfate, concentrating resulting to ethyl 2-chloro-2-propenate-containing carfentrazone-ethyl derivative of formula (iv), performing catalytic hydrogenation with 5-20 wt.% hydrogen and 5-20 wt.% palladium/carbon catalyst in the organic solvent at 25-35 degrees C.
NOVELTY - A thermophilic Streptomyces thermocarboxydus strain CF1 (CGMCC 6873), is new.    USE - The thermophilic S.thermocarboxydus strain CF1 (CGMCC 6873) is useful in animal manure which is useful as fertilizer (all claimed), and for controlling pathogens and parasites in animal.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing biological agent, involves culturing the above-mentioned strain in liquid fermentation medium; and (2) animal manure used as fertilizer, comprising the above-mentioned strain, Bacillus subtilis, and B.megaterium.
NOVELTY - A Stenortrophomonas maltophilia JYD-4 strain deposited under CCTCC NO: M2012264, is new.    USE - The strain is useful for promoting Taxus chinersis var. (claimed), preferably for preparing microbial inoculum for promoting growth of southern yew seedling.    ADVANTAGE - The strain has strong degradation ability.
NOVELTY - Method for cultivating crystal grape, involves processing groove, adding 200-220 times bordeaux, where the groove volume is 100x100x80cm, applying organic fertilizer, selecting branch with leaf bud, where length of the grape branch is 15-25 cm, and lower end of the branch is inclined at 30-60 degrees , planting branch, performing pruning process and applying fertilizer to grape every 5-25 days, where the fertilizer comprises 70-80 pts. crushed straw, 30-40 pts. dried chicken, 5-15 pts. soybean, 5-10 pts. beans, 5-10 pts. dried manure and 20-30 pts. cooked beans.    USE - The method is useful for cultivating crystal grape (claimed).    ADVANTAGE - The method controls diseases and insect pests, reduces usage of chemical pesticide, and is environmentally-friendly.
NOVELTY - The utility model claims a high efficiency organic fertilizer production line, orderly comprising a feeding device, a feeding hopper is connected with the inlet's, with the first frame's solid-liquid separating machine is connected with the second frame with the solid-liquid separating machine's connection with the second frame's connected mixing and stirring device, a third feeding device is connected with the mixing's with the third frame connecting's filling device. The production efficiency is high, it does not need manual transportation, saves labour.
NOVELTY - Processing manure into organic fertilizers, comprises disinfection of manure (with simultaneous crushing) which occurs in variable electromagnetic field in flowing mode.    USE - The method is useful for processing manure into organic fertilizers (claimed).
NOVELTY - The apparatus has front-end which is connected with upper portion of processing tank (33). A flow volume adjustment portion is provided to adjust flow volume of gas and liquid to constantly maintain the height of gaseous phase in processing tank. The injection direction of mixed fluid from injection portion is orthogonally crossed on central axis of processing tank. The branch pipe (322a-322d) is configured to inject mixed fluid from branch pipe, so that the bubble in injected mixed fluid arrives in bottom portion of processing tank.    USE - Apparatus e.g. liquid processing apparatus for processing fluid such as bathtub water, toilet water, drink e.g. wine, lake water, hot-spring water and drinking water, used in industry, agriculture, fishery, service industry. Can also be used for removing gas such as methane gas, chlorine, sulfur-containing gas, carbon monoxide such as volatile carbonization gas, hydrogen sulfide, oxygen and nitrogen dissolved into liquid.    ADVANTAGE - The structure of the fluid processing apparatus is simplified easily, so that the dissolved gas can be removed from to-be-processed water efficiently. The cost of the apparatus can be reduced. The space occupied by the fluid processing apparatus can be reduced. The production of the apparatus can be improved. The growth defect by the oxygen deficiency in the middle of the planter of the water culture cultivation can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the fluid processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the liquid processing apparatus. (Drawing includes non-English language text)    Deaeration process unit (30)    Processing tank (33)    Exhaust valve (34)    Main pipe (321)    Branch pipes (322a-322d)
NOVELTY - Obtaining biodiesel by transesterification of rape oil in supercritical methanol, where the rape oil is processed with volumetric speed of 0.2-4.2 ml/minute and methanol with bulk speed of 0.2-3.9 ml/minute and supplied by respective dispensing pumps through unit of emergency returning excess pressure in heater, from which mixture, heated to 120-200 degrees C, directed into tubular type thermostatically controlled at 200-300 degrees C flowing reactor with inner diameter of pipe of 4-8 mm and length of 150-300 mm.    USE - The method is useful for obtaining biodiesel by transesterification of rape oil in supercritical methanol (claimed).    DETAILED DESCRIPTION - Obtaining biodiesel by transesterification of rape oil in supercritical methanol, where the rape oil is processed with volumetric speed of 0.2-4.2 ml/minute and methanol with bulk speed of 0.2-3.9 ml/minute and supplied by respective dispensing pumps through unit of emergency returning excess pressure in heater, from which mixture, heated to 120-200 degrees C, directed into tubular type thermostatically controlled at 200-300 degrees C flowing reactor with inner diameter of pipe of 4-8 mm and length of 150-300 mm, where in reactor pressure is maintained at 20-30 MPa, further transesterification mixture of products is cooled to a temperature of 15-25 degrees C via descending water refrigerator, cooled mixture is maintained before stratification for separation of methanol and glycerin from end product.
NOVELTY - Power-engineering multifunctional complex for processing biomass, comprises a gasifier intended to produce generator gas, gas-piston power unit for production of electrical energy, programmer with computer connected to the actuator of all elements of complex with the measuring equipment and designed for controlling the normal operation of all devices of complex, where the complex contains a device for primary crushing of biomass, pelletizing ground biomass, torrefication of bio-pellets, and synthesis of liquid propellants.    USE - The power-engineering multifunctional complex is useful for processing biomass (claimed).    DETAILED DESCRIPTION - Power-engineering multifunctional complex for processing biomass, comprises a gasifier intended to produce generator gas, gas-piston power unit for production of electrical energy, programmer with computer connected to the actuator of all elements of complex with the measuring equipment and designed for controlling the normal operation of all devices of complex, where the complex contains a device for primary crushing of biomass, device for fine grinding of biomass, device for pelletizing of ground biomass with obtaining bio-pellets, device for torrefication of bio-pellets, device for synthesis of liquid propellants, and also line of supply of electric power to all devices and lines of supply of waste gas of power unit into the gasifier and torrefication device.
NOVELTY - A method comprises capturing carbon dioxide from a carbon dioxide source; fixing the carbon dioxide; converting the fixed carbon dioxide into a biomass; and preparing a high value material.    USE - The method is used for preparing a high value material (claimed).    ADVANTAGE - Methods and apparatus that reduce, eliminate, and/or mitigate greenhouse gas production are provided.
NOVELTY - Thermophilic bacterial chimera comprising a fusion of two species of Clostridia, where the fusion comprises Clostridium thermobutanolicum deposited with the ATCC on Dec. 22, 2011 and designated as MF 14ACpTC, is new.    USE - The thermophilic bacterial chimera is useful: for breaking down a biomass containing complex carbohydrates into glucose and converting glucose into biofuel; for breaking down a cellulosic biomass into glucose, convert glucose into butyric acid, carbon dioxide and hydrogen and, convert butyric acid into butanol at thermophilic temperatures of 45-65 degrees C; and in a single-step, single-vessel method of converting a biomass into a biofuel, where the biofuel is butanol (preferred), methanol, ethanol, propanol or methane gas (all claimed).    ADVANTAGE - The method allows biochemical digestions and fermentation in one single vessel and single step, and thus is cost effective, eliminates the need for multiple step digestion and fermentation processes requiring multiple chambers, reduces the rate limiting steps where increasing accumulation of alcohol, butanol and other substances become toxic to the very bacteria that produce these biofuels, and eliminates the need for periodic stoppage and restarting of the process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a single-step, single-vessel method of converting a biomass into a biofuel, comprising: (a) combining a biomass comprised of complex carbohydrates and a thermophilic anaerobic biocatalyst microorganism in a single reaction chamber, where the thermophilic anaerobic biocatalyst microorganism comprises the Clostridium thermobutanolicum which is designated as MF14ACpTC; (b) permitting the biocatalyst microorganism to digest complex carbohydrates found in the biomass into glucose and other monosaccharides; and (c) fermenting the resultant glucose and other monosaccharides into a biofuel.
NOVELTY - Improving catalyst resistance of a catalyzed filter element against poisoning by alkali metals or alkali metal compounds, involves affixing an alkaline powder on surface of the filter element prior to the filter element, and contacting with poisonous alkali metals or alkali metal compounds.    USE - The methods are useful for improving catalyst resistance of catalyzed filter element against poisoning by alkali metals or alkali metal compounds; for preparing catalyzed filter being resistant against poisoning by alkali metals or alkali metal compounds; and for cleaning flue gas containing alkali metals and/or alkali metal compounds. The alkali metal resistant catalyzed filter element is useful for cleaning flue gas from combustion of biomass, waste incineration and glass manufactory (all claimed).    ADVANTAGE - Catalyzed filter element is provided with improved alkali metal resistance for the removal of particulate matter and environmental or health harmful compounds from flue or off-gases containing alkali metals or alkali metal compounds.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing catalyzed filter being resistant against poisoning by alkali metals or alkali metal compounds, involving affixing an alkaline powder on surface of the filter element; and    (2) a method of cleaning flue gas containing alkali metals and/or alkali metal compounds, involving affixing an alkaline powder on surface of a catalyzed filter element prior to the catalyzed filter element is brought into contact with the flue gas.
NOVELTY - Preparation of a thiazole compound (I), involves: reacting aldehyde derivative (II) with amide compound (III) in a solvent containing formic acid, where the process does not use any phosphorus-containing catalyst.    USE - For preparation of a thiazole compound (claimed) used as sedative and hypnotic drugs; and as anticancer drugs.    ADVANTAGE - The method has a high yield, easily-controlled reaction conditions and does not use any catalyst toxic or hazardous to environment, so it is economic, environmental friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparation of a thiazole compound of formula (I), involves: reacting a compound of formula (II) with a compound of formula (III) in a solvent containing formic acid, where the process does not use any phosphorus-containing catalyst.    R1, R'1 and R2=optionally substituted 1-10C hydrocarbyl or H;    R3=optionally substituted 1-10C hydrocarbyl, H, 5- or 6-membered heterocyclic group or 5- or 6-membered heteroaryl;    R4=optionally substituted 1-10C acyl or H;    R'4=optionally substituted 1-10C hydrocarbyl or H;    X=H, 1-10C acyl or group of formula (i).    An INDEPENDENT CLAIM is included for preparation of a thiazole compound of formula (Ia), involving: reacting a compound of formula (IIa)/(IIb) with a compound of formula (IIIa) in a solvent containing formic acid, where the process does not use any phosphorus-containing catalyst.    R5 and R'5=H, formyl or acetyl.
NOVELTY - The processing system has a suspensible organic substance separation apparatus (10) which separates suspensible organic substance from to-be-processed water containing suspensible organic substance. A sludge anaerobic digester (20) carries out anaerobic digestion of the suspensible organic substance separated by suspensible organic substance separation apparatus. A first transfer route (R1) through which the separated liquid from which the suspended organic substances is removed in suspensible organic substance separation apparatus is supplied to nitritation apparatus (30).    USE - Processing system of suspensible organic matter containing wastewater.    ADVANTAGE - The first transfer route through which the separated liquid from which the suspended organic substances is removed in suspensible organic substance separation apparatus is supplied to nitritation apparatus. Thus, the improved processing system of efficient suspensible organic matter containing wastewater can be provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing method of the suspensible organic matter containing wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the processing system of suspensible organic matter. (Drawing includes non-English language text)    Suspensible organic substance separation apparatus (10)    Sludge anaerobic digester (20)    Nitritation apparatus (30)    Autotrophic denitrifying apparatus (40)    First transfer path (R1)
NOVELTY - Method for producing ethanol from biomass, involves mixing transformed xylose-utilizing yeast to over-express gene for an acetic acid response transcription factor with saccharified biomass, and culturing the yeast.    USE - The method is useful for producing ethanol from biomass (claimed), preferably lignocellulosic biomass e.g. rice straw which does not compete with food wheat straw, and waste material which is useful for preventing global warming.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for transformed xylose utilizing yeast, which is obtained by the above-mentioned method.
NOVELTY - Hydrolysis method of cellulose involves contacting cellulose and liquid obtained by injecting gas in pressurized hot water, and hydrolyzing cellulose. The pressure of the liquid is 0.2-20 Mpa, and the temperature of liquid is 120-300 degrees C.    USE - Hydrolysis method of cellulose used for manufacturing glucose and 5-(hydroxymethyl)-2-furaldehyde (all claimed) used as fossil fuel and biofuel for chemical and pharmaceutical application, and oligosaccharide used as raw material of ethanol.    ADVANTAGE - The method enables efficient hydrolysis of cellulose. The glucose and 5-(hydroxymethyl)-2-furaldehyde are manufactured with high yield, using the hydrolysis method of cellulose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of glucose, which involves hydrolyzing cellulose; and    (2) manufacture of 5-(hydroxymethyl)-2-furaldehyde, which involves hydrolyzing cellulose.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of hydrolysis apparatus.    Hydrolysis apparatus (1)    Gas-liquid mixer (10)    Injection nozzle (11)    Reaction container (20)    Flow paths (F1,F2,F3,F4,F5)
NOVELTY - A cephalosporin intermediate penicillin sulfoxide preparation method involves adding salt solution in penicillin fermentation extracting solution at a temperature of 0-20 degrees C to obtain water phase, where pH value is 6.5-7.5. The water phase is decolored, decompressed and concentrated. The concentrated phase is processed in an aluminum oxide column to obtain the penicillin industrial salt solution. The penicillin industrial salt solution is heated to 0-15 degrees C, subjected to an oxidation treatment using peroxyacetic acid, filtered and washed to obtain the finished product.    USE - Method for preparing a cephalosporin intermediate penicillin sulfoxide.    ADVANTAGE - The method enables preparing the cephalosporin intermediate penicillin sulfoxide in a simple and economical manner with high yield and low energy consumption.    DETAILED DESCRIPTION - A cephalosporin intermediate penicillin sulfoxide preparation method involves adding salt solution in penicillin fermentation extracting solution at a temperature of 0-20 degrees C to obtain water phase, where pH value is 6.5-7.5. The water phase is decolored, decompressed and concentrated. The concentrated phase is processed in an aluminum oxide column to obtain the penicillin industrial salt solution. The penicillin industrial salt solution is heated to 0-15 degrees C and pH value is adjusted to 0.9-1.2 using diluted acid. The heated salt solution is subjected to an oxidation treatment using peroxyacetic acid, filtered and washed to obtain the finished product.
NOVELTY - Method for cultivating agaric using pig manure residues involves using traditional fungus culture medium containing pig manure residues after solid-liquid separation instead of wheat bran and wooden meal, where the pig manure residue is washed by using flushing water column, adding the washed pig manure residue to concentrated sewage collection tank after mixing, and collecting the obtained product including the edible fungus, black fungus, and Auricularia polytricha.    USE - The method is useful for cultivating agaric using pig manure residues (claimed).    ADVANTAGE - The method enables to prepare product cost-effectively, and environmentally-friendly, and which improves the utilization value of pig waste residues.
NOVELTY - Substrate comprises agriculture and forestry waste, urea-formaldehyde, wood charcoal powder, mitogens, and ammonium chloride.    USE - The substrate is useful for culturing plant (claimed).    ADVANTAGE - The substrate utilizes waste wood chips, straw and agricultural waste, is cost-effective and environmentally-friendly, and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing substrate, which involves (a) crushing the agriculture and forestry waste, and sieving the crushed components to obtain powder of 2-10 mm, (b) mixing the agriculture and forestry waste, urea-formaldehyde, wood charcoal powder, mitogen and ammonium chloride, (c) stirring the mixture, pressing the mixture, (d) molding the mixture, (e) placing the mixture in microwave oven, and performing sterilization at 80-90 degrees C for 4-6 minutes, and (e) air-drying the obtained product using hot air tunnel, and evaporating residual water.
NOVELTY - A non-chemical pesticide is prepared by mixing diesel oil, vegetable juice and water at ratio of 1:15:100. The vegetable juice comprises tomato, pumpkin, scallion and garlic, and is prepared by extracting juice in tomato, pumpkin, scallion and garlic and filtering to obtain pure vegetable juice.    USE - Method of preparing non-chemical pesticide (claimed).    ADVANTAGE - The method has low cost and no pesticide product residue, no pollution to the environment and no damage to human. The prepared pesticide is environment-friendly and safe.
NOVELTY - Kitchen organic matter processing self-purifying system, the washing vessel is installed under pulverizer of organic liquid guide pipe is connected with the organic matter, organic matter processing box comprises a decomposing area, purifying area and a clapboard, decomposing area is provided with a decomposing tank, solid-liquid separating tube, in the purifying area is provided with a purifying tank, contact material, an oxygen pipe, pipe, baffle plate, solid-liquid separation pipe is composed of decomposition groove passes through the partition and the purifying area is connected with the kitchen organic matter processing self-purification system which is not limited by time, not only can simple and fast processing organic kitchen garbage, but also can maximum extent up to reduce pollution to the environment's.
NOVELTY - Preparation of soil-less culture substrate comprises drying and roasting solid material with particle size of 6-9 mm, uniformly mixing with chicken manure to obtain solid substrate, spraying nutrient solution, uniformly mixing and naturally fermenting at 20-30 degrees C for 10-15 days.    USE - Method for preparing soil-less culture substrate (claimed).
NOVELTY - Reducing carbon dioxide emission in co-production of mineralized carbon dioxide and potassium sulfate using potassium feldspar-calcium sulfate by curing, comprises grinding potassium feldspar mineral powder with calcium sulfate-containing industrial solid waste (e.g. phosphogypsum and desulfurized gypsum), molding, carrying out high-temperature activation reaction using carbon dioxide mineralized calcined residue and separating to obtain calcium carbonate-containing mineralization slag and water-soluble potassium sulfate fertilizer.    USE - The method is useful for: reducing carbon dioxide emission in co-production of mineralized carbon dioxide and potassium sulfate; and produces calcium carbonate-containing aluminosilicate used as cement raw material, and potassium sulfate used as fertilizer (all claimed).    ADVANTAGE - The method is environmentally friendly and has triple effect.
NOVELTY - A central water network block nonpoint source pollution control system comprises intercepting branch canal system (2), rain sewage distributing well (3), ecological trunk canal (4), land-constructed wetland depth processing system (5), and buffer fence (6). The system further comprises recycling flow weir, waste-recycling water storage tank channel network, water front ecological slope, garbage collecting system, septic tank, high temperature pile fertilizer kettle, and garbage cleaning facilities.    USE - Central water network block nonpoint source pollution control system.    ADVANTAGE - The system has stable process and treatment and high ecological landscape value, maintains ecological balance, is simple and easy to construct, and has low investment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the construction of system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of central water network block nonpoint source pollution control system.    Intercepting branch canal system (2)    Rain sewage distributing well (3)    Ecological trunk canal (4)    Land-constructed wetland depth processing system (5)    Buffer fence (6)
NOVELTY - A multifunctional turner comprises guide rail (1), machine frame (2), walking driving device (3), turning main shaft (4), and turning tooth rake (5). The turner further comprises turning driving device, outer cover, exhaust channel, and odor processing device.    USE - Multifunctional turner used for absorbing odor, spraying deodorant, and inoculating.    ADVANTAGE - The turner inhibits release of odor.    DESCRIPTION OF DRAWING(S) - The drawing shows as schematic diagram of multifunctional turner.    Guide rail (1)    Machine frame (2)    Walking driving device (3)    Turning main shaft (4)    Turning tooth rake (5)
NOVELTY - Preparation of organic-inorganic compound fertilizer comprises concentrating raw biogas slurry at less than or equal to 100 degrees C to water content of 20-25%; drying and grinding diatomite, sieving through 100-120 mesh screen; uniformly mixing yellow phosphorus furnace gas de-dusting ash and diatomite at a mass ratio of 7:3-9:1 to obtain solid mixture, mixing with biogas slurry at mass ratio of 1:3-1:6, uniformly stirring; drying to less than 10% water content at 105 degrees C.    USE - Method for preparing organic-inorganic compound fertilizer (claimed).    ADVANTAGE - The fertilizer is environment-friendly.
NOVELTY - Foliar fertilizer comprises mixed liquid fertilizer and effective microorganisms (EM) expanding liquid. The mixed liquid fertilizer comprises calcium chloride aqueous solution, calcium nitrate aqueous solution, and potassium nitrate aqueous solution. The EM expanding liquid comprises molasses, EM stock solution and water.    USE - Foliar fertilizer used for tomato (claimed).    ADVANTAGE - The method is simple and low cost. The fertilizer has balanced nutrition, promotes growth of tomato plants, improves sugar content and yield, and greatly reduces tomato navel rot disease incidence.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising uniformly mixing calcium chloride aqueous solution, calcium nitrate aqueous solution, and potassium nitrate aqueous solution to obtain mixed liquid fertilizer; dissolving molasses and EM stock solution in water at constant temperature to obtain EM expanding solution; uniformly mixing EM expanding solution with mixed liquid fertilizer, and culturing at constant temperature.
NOVELTY - Purifying 1,8-cineole comprises (a) introducing 1,8-cineole and limonene containing raw material oil, acetic acid or acetic acid aqueous solution and catalyst into a reaction bottle, (b) heating, stirring and reacting, and (c) filtering the reaction liquid after the reaction, recycling the catalyst, rectifying the oil phase under vacuum.    USE - The method is useful for purifying 1,8-cineole (claimed).    ADVANTAGE - The method reduces impurity content to 0.2-1.1%; does not affect alpha -terpinene, gamma -terpinene and alpha -terpineol during the rectification process; and is economical and environmentally friendly.
NOVELTY - The utility model claims a power-free pure ecological one device, which is used for recycling method of wasted metal sludge in the sewage processing tank's precipitate sludge's to be taken after filtering and recycling, comprising a sludge containing's recovery cylinder body is connected between the mud in the sewage processing pool bottom part and the inner wall of the cylinder body, the mud and the sludge into the sludge pump's in the cylinder body, bag is set inside the bottom of the cylinder body and periphery's outer cylinder, a sludge pump is set sewage processing tank, upper bottom surface and side wall's inner wall of the cylinder body is provided with a water leakage hole, the bottom of the outer cylinder body and the inner cylinder body is formed in the cylinder body in the sludge and sewage's's gap, the outer cylinder body is provided with the sewage in the sewage recycling pipe's sewage processing pool. By hot stack fertilizer, using heat generated in the process of composting's heat can kill the bacterial's, and sludge from domestic sewage, does not contain non-degradable's toxic organic matter and heavy metal ion, compost can be relieved by the farmer's green or field and the material recycling's.
NOVELTY - This utility model claims one kind of compound organic fertilizer production system, comprising a fermentation tank, said fermenter's two sides of the top are respectively provided with one strip turning rail, said upper rail is provided with turning dumper's outlet end of said fermentation tank is connected with the collecting tank by the conveyor belt, screening device and packaging device is connected with the said stack dumper is provided with a vertical lifting mechanism and axial-flow fan cooling mechanism, said fermentation tank is provided with a temperature sensor and an electric heating mechanism, the utility model's advantages as follows: fermentation's according to different seasons and stage, the air quantity, wind speed and temperature control, taking micro organism of solid state fermentation's so as to meet requirement of fermentation temperature and oxygen, promoting propagation's, shortens fermentation's production time to heat, it has high production efficiency and can continuously flow production, fertilizers completely, fermenting quality and power consumption.
NOVELTY - This utility model claims one kind of processing equipment for biological organic fertilizer, comprising a crushing device, mixing device and mixing and pelletizing device's are connected in turn, a crushing device is provided with a grain feeding hopper and a feeding hopper, assistant material grain feeding hopper and the feeding hopper are respectively connected with the assistant material to be crushed material, crushing material is orderly connected with the crusher, sieving, dosing device is provided with a mixing tank, inlet end's bin and sieving machine is connected, the outlet end's storage bin by the spiral and batching scale, mixing and pelletizing device is provided with a double-ribbon mixer, the inlet end's double-ribbon mixer by screw conveyer and batching scale, the outlet end's double-ribbon mixer's machine is connected with the inlet end, the inlet end's double-ribbon mixer is further connected with a trace element dosing machine, advantages's This utility model has the following advantages: it realizes the production line operation, Process parameters are easy to control, the product quality is stable, the production efficiency is high and small floor area.
NOVELTY - The utility model claims an organic fertilizer stacking's wheel with telescopic legs, comprising a machine frame, multiple turnover is set on the machine frame upper's turning shaft, the turning shaft is set up's, said upper frame is provided with a motor driving the first turning shaft's rotation, said frame's four corners at the bottom are equipped with mobile roller wheel, said upper frame is provided with a front end of the machine frame to drive's two mobile's second motor roller to rotate, the bottom of said frame is provided with a fixing frame's, said mobile rolling wheel fixing frame is set on the upper bottom of said fixing frame is provided with a telescopic's's. It can effectively reduce's mobile roller upper stacking's abrasion and prolongs service life's mobile roller, the running roller change's frequency and saves labour.
NOVELTY - The utility model claims low energy consumption organic fertilizer stacking, comprising a machine frame, multiple turnover is set on the machine frame upper's turning shaft, the turning shaft is set up's, said upper frame is provided with a motor driving the first turning shaft's rotation, said frame's four corners at the bottom are equipped with mobile roller wheel, said upper frame is provided with a front end of the machine frame to drive's two mobile idler wheel's second motor. Structure is simple, the operation is simple, it does not need the worker sits on the upper machine operation, and can greatly reduce the energy consumption.
NOVELTY - This utility model claims one kind of bar buttress type tobacco organic fertilizer fermenting technology platform, comprising a fermentation platform is provided with multiple parallel strip-shaped's platform in the fermentation compost platform (1), the composting platform (1)'s middle position is opened with the ventilation groove (2), is provided with an opening cover plate up the ventilation groove (2) (3). The utility model in the process of fermenting, ventilation groove can vent, oxygen supplying effect, because the beneficial organism colony's HM FERMENT base inside belongs to the aerobic strain, only the fermented substance better decomposed under the enough oxygen; so as to improve the biological organic fertilizer fermenting effect and quality's, at the same time it can has good draining effect and avoids the rain in the southwest caused by too much fertilizer's humidity;
NOVELTY - This utility model claims one kind of decomposing tank, comprising a cylindrical decomposition mechanism and substantially perpendicular to said decomposition mechanism's feeding mechanism, said feeding mechanism and decomposition mechanism for the animal body from the feeding inlet end's mechanism the decomposition mechanism. The utility model claims a decomposing pool's upper-based process is the biological decomposition's, barrier anti-oxidation material's price, and ground source heat source is heat source, there is no need for long time monitoring, can effectively reduce the animal's for producing harmful gas pollution to the air's, it can obviously reduce leakage's pollution to the underground water and the environment, is easy to manage;
NOVELTY - This utility model claims one kind of solid organic waste harmless quickly, comprising an electric control system and a main body part, said electric control system is composed of an electric control box, an electric motor, a reduction box, a coupler and a bearing, said bearing and the main shaft's main body part, said main body part comprises a box body, a movable baffle plate, a main shaft, a paddle, a feed port and a discharge port, said box body is cylindrical, said main shaft is located in the centre shaft's box body, said paddle along the spiral, said feeding port is located on the box body close to the motor side's top part, said discharge hole far away from the surface of the side wall of the box's motor; said mobile baffle plate is at the discharge hole. The utility model has solid organic waste harmless ferment machine uses the paddle turning, small abrasion and low maintenance cost, saving energy, using gear box control paddle's rotation speed per minute 3-5 ring, it is good for air flow, but also is good for fermentation's to the fermentation speed can reach 25 per day.
NOVELTY - Breeding animals involves uniformly spraying waterproof coating on surface of floor, placing far infrared composite material on floor surface, adding water into container for livestock, then adding effective microorganism, uniformly stirring, spraying EM strain feed, sealing the fermentation process for 8-24 hours, then using livestock excrement as organic fertilizer, or supplying ecological fertilizer as raw material.    USE - The method is useful for breeding animals, preferably livestock (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method of breeding animals, involves sterilizing field's floor, wall, ceiling and facilities including metal tube and net, uniformly spraying waterproof coating on surface of floor, placing far infrared composite material on the floor surface, adding water into container for livestock, then adding effective microorganism (EM) flora to prepare bacterial liquid, diluting bacterial liquid using sterile water, uniformly stirring, spraying EM strain feed at 25 degrees C for 3-5 days, sealing the fermentation process for 8-24 hours, then using livestock excrement as organic fertilizer, or supplying ecological fertilizer as raw material.
NOVELTY - A tropisetron citrate (I), is new.    USE - New tropisetron citrate (claimed).    ADVANTAGE - The tropisetron citrate having high-purity is efficiently manufactured by environmentally-friendly process.    DETAILED DESCRIPTION - A tropisetron citrate of formula (I), is new.
NOVELTY - An oxiracetam lyophilized freeze-dried powder injection is prepared from oxiracetam, D-sorbitol, mannitol and water.    USE - Oxiracetam lyophilized freeze-dried powder injection (claimed).    ADVANTAGE - The oxiracetam lyophilized freeze-dried powder injection is economically prepared with high productivity, under reduced energy consumption, by environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of oxiracetam lyophilized freeze-dried powder injection, which involves taking 2400 ml water, adjusting the temperature to 55-65 degrees C, adding oxiracetam, D-sorbitol and mannitol, stirring to obtain solution, cooling the solution to 35 degrees C, adding medicinal charcoal, stirring and absorbing, decarburizing, filtering, adjusting pH of filtrate to 5-5.5 using 5% sodium hydroxide, adding 3000 mL water, filtering using 0.22 mu m microporous membrane to obtain fine filtrate, qualifying the fine filtrate, filling into vial, sealing, freeze-drying, and packing.
NOVELTY - A rough surface of pearl shell is removed, and crushed to pearl shell fine powder. The water and pearl shell fine powder are mixed, to form suspension. The edible alkali and water are mixed, to obtain edible alkali solution. The taurine and water are mixed, and taurine is dissolved in water, to obtain taurine solution. The edible alkali solution is heated and added to suspension and mixed. The suspension and taurine solution are mixed and dissolved, to form pearl shell solution. The pearl shell solution is calcined and dried, to obtain soluble pearl calcium product.    USE - Preparation of soluble pearl calcium product used for medicine, food and cosmetics.    ADVANTAGE - The method enables safe and economical preparation of soluble pearl calcium product with reduced energy consumption, without environmental pollution.    DETAILED DESCRIPTION - A rough surface of pearl shell is removed, and crushed to pearl shell fine powder of 100-300 meshes. The water and pearl shell fine powder in weight ratio of 8-10:5-7 are mixed, to form suspension. The edible alkali and water in weight ratio of 1-3:10-12 are mixed, to obtain edible alkali solution. The taurine and water in weight ratio of 1-3:10-12 are mixed, and taurine is dissolved in water, to obtain taurine solution. The edible alkali solution is heated at 55-85 degrees C and added to suspension such that the volume ratio of edible alkali solution and suspension is 1:3-6 and mixed at 55-85 degrees C for 60-72 hours, further mixed for 2-3 hours and 5-10 minutes. The suspension and taurine solution in volume ratio of 1:3-6 are mixed and dissolved, to form pearl shell solution. The pearl shell solution is calcined under vacuum at 60-85 degrees C and dried at 90-100 degrees C, to obtain soluble pearl calcium product.
NOVELTY - Organic fertilizer preparation comprises cleaning Enteromorpha, drying until water content of 40-45%, adding Bacillus megaterium and composting for 1 day, and adding yeast and aerobically fermenting for 2-3 days.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method converts waste into valuable product and is environment-friendly. Decomposition temperature reaches 70 degrees C, which favors Enteromorpha toxin decomposition and increases nutrition and disease-resistant of fertilizer.
NOVELTY - Recycling golden needle mushroom residue comprises analyzing needle mushroom residue to determine cellulose, protein, amino acid and trace element contents; screening edible fungus strain for cultivation and screening degradable mushroom residue; and stacking mushroom residue, primary fermenting, and performing secondary fermentation to produce organic fertilizer.    USE - Method for recycling golden needle mushroom residue used for producing organic fertilizer useful as soilless substrate or for application to soil for vegetable cultivation (claimed).    ADVANTAGE - The method reduces mushroom production cost, improves mushroom residue utilization rate, increases vegetable production, and promotes social employment.
NOVELTY - Method for preparing fertilizer, involves (a) uniformly mixing passion fruit leaves and kitchen waste in fermentation bed, adjusting carbon/nitrogen ratio of the mixture to 30-40%, and adjusting moisture content of the mixture to 55-65%, (b) mixing bacterial enzyme and wheat bran in a ratio of 1:3-7 and adding the mixture to the fermentation bed and stacking the bed, and (c) piling up the stacking material, covering the pile using film, turning up the pile once for every 5-15 days, and composting the fertilizer for 50-70 days.    USE - The method is useful for preparing fertilizer which is useful for passion fruit (claimed).    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - Organic fertilizer production comprises drying and crushing sea cucumber intestines; and mixing 10-15 pts. wt. dry sea cucumber intestine powder, 20-40 pts. wt. fresh livestock and poultry manure, 40-50 pts. wt. crushed crop straw, 10-15 pts. wt. humic acid and 0.5-1 pts. wt. Bacillus megaterium, and composting at 30-50 degrees C for 5-7 days.    USE - Method for producing organic fertilizer (claimed) useful as base fertilizer or top dressing.    ADVANTAGE - The method converts waste into valuable product, i.e. fertilizer which can completely replace chemical fertilizer.
NOVELTY - Organic fertilizer production comprises drying sea cucumber cooking liquid; and mixing 5-10 pts. wt. sea cucumber cooking liquid dry powder, 10-50 pts. wt. chicken manure, 10-20 pts. wt. walnut shell powder, 20-50 pts. wt. crushed crop straw, 10-15 pts. wt. rice bran and 0.5-1 pts. wt. Bacillus laterosporus, and composting at 30-50 degrees C for 2-3 days.    USE - Method for producing organic fertilizer (claimed) useful as base fertilizer or top dressing.    ADVANTAGE - The method converts waste into valuable product, i.e. fertilizer which can completely replace chemical fertilizer.
NOVELTY - Hawthorn tree base fertilizer preparation comprises crushing dry dairy manure, dry pig manure, plant straw, Chinese trumpet creeper, tea seed cake, distiller's grain and soy sauce residue, uniformly mixing with plant ash and fermentation agent, adding water, and sealing and fermenting to obtain organic-inorganic compound fertilizer; and crushing urea, monoammonium phosphate, potassium sulfate, chelated iron amino acid, chelated calcium amino acid, chelated magnesium humic acid and chelated copper humic acid into powder, and uniformly mixing with compound fertilizer and amino acid waste liquid.    USE - Method for preparing base fertilizer used for hawthorn tree (claimed).    ADVANTAGE - The fertilizer improves disease resistance, drought resistance and cold resistance of hawthorn tree; and increases hawthorn fruit quality and production yield.    DETAILED DESCRIPTION - Hawthorn tree base fertilizer preparation comprises:    (A) crushing 24-26 wt.% dry dairy manure, 28-30 wt.% dry pig manure, 10 wt.% plant straw, 8 wt.% Chinese trumpet creeper, 3 wt.% tea seed cake, 3 wt.% distiller's grain and 3 wt.% soy sauce residue; adding 4 wt.% plant ash and 1 wt.% fermentation agent; uniformly mixing; adding water; and sealing and fermenting for 28-30 days, preferably 29 days to obtain organic-inorganic compound fertilizer; and    (B) crushing 4 wt.% urea, 3 wt.% monoammonium phosphate, 3 wt.% potassium sulfate, 0.4 wt.% chelated iron amino acid, 0.4 wt.% chelated calcium amino acid, 0.1 wt.% chelated magnesium humic acid and 0.1 wt.% chelated copper humic acid into powder; and uniformly mixing with organic-inorganic compound fertilizer and 3 wt.% amino acid waste liquid.
NOVELTY - Jujube tree base fertilizer preparation comprises fermenting dry dairy manure, dry pig manure, rapeseed cake, castor cake, peanut straw and shells, grass leaves, distiller's grains, monosodium glutamate residue, dry pond sludge, fermentation agent and water; and uniformly mixing with crushed urea, diammonium phosphate, potassium chloride, chelated iron amino acid, chelated calcium amino acid, chelated magnesium amino acid, chelated zinc humic acid and chelated molybdenum humic acid.    USE - Method for preparing base fertilizer used for jujube tree (claimed).    ADVANTAGE - The fertilizer improves disease resistance, drought resistance and cold resistance of jujube tree; and improves jujube fruit quality and production yield.    DETAILED DESCRIPTION - Jujube tree base fertilizer preparation comprises:    (A) crushing 18-20 wt.% dry dairy manure, 30-32 wt.% dry pig manure, 6 wt.% rapeseed cake, 5 wt.% castor cake, 6 wt.% peanut straw and shells, 6 wt.% grass leaves, 4 wt.% distiller's grains, 3 wt.% monosodium glutamate residue and 5 wt.% dry pond sludge; adding 1 wt.% fermentation agent and water; uniformly mixing; and sealing and fermenting for 25-30 days, preferably 28 days to obtain organic fertilizer; and    (B) crushing 4 wt.% urea, 4 wt.% diammonium phosphate, 5 wt.% potassium chloride, 0.3 wt.% chelated iron amino acid, 0.3 wt.% chelated calcium amino acid, 0.1 wt.% chelated magnesium amino acid, 0.2 wt.% chelated zinc humic acid and 0.1 wt.% chelated molybdenum humic acid into powder; and uniformly mixing with organic fertilizer.
NOVELTY - Preparation of a fertilizer comprises preparing an organic compound fertilizer by fermenting 30-32 wt.% dry pig manure, 8-10 wt.% dry chicken manure, 10 wt.% corn straw, 5 wt.% cottonseed, 13 wt.% river mud, 1 wt.% organic manure fermentation agent, 4 wt.% plant ash, and water for 20-25 days; and uniformly mixing with crushed 3 wt.% sodium alginate, 5 wt.% urea, 7 wt.% diammonium phosphate, 6 wt.% potassium sulfate, 0.3 wt.% amino acid chelated iron, 0.1 wt.% amino acid chelated magnesium, 0.4 wt.% chelated calcium, and 0.2 wt.% humic acid chelated copper.    USE - Method for the preparation of a fertilizer used for persimmon (claimed).    ADVANTAGE - The fertilizer improves persimmon fruit quality.    DETAILED DESCRIPTION - Preparation of a fertilizer comprises:    (A) preparing an organic compound fertilizer by crushing 30-32 wt.% dry pig manure, 8-10 wt.% dry chicken manure, 10 wt.% corn straw, 5 wt.% cottonseed, and 5 wt.% castor cake; adding 13 wt.% river mud, 1 wt.% organic manure fermentation agent, 4 wt.% plant ash; uniformly mixing, and adding water; and fermenting for 20-25 days, preferably 22 days;    (B) crushing 3 wt.% sodium alginate, 5 wt.% urea, 7 wt.% diammonium phosphate, 6 wt.% potassium sulfate, 0.3 wt.% amino acid chelated iron, 0.1 wt.% amino acid chelated magnesium, 0.4 wt.% chelated calcium, and 0.2 wt.% humic acid chelated copper; and    (C) uniformly mixing with organic compound fertilizer.
NOVELTY - A bio-organic fertilizer comprises sludge, pig manure, and straw fermentation mixture.    USE - A bio-organic fertilizer.    ADVANTAGE - The fertilizer is inexpensive.
NOVELTY - Preparation of a fertilizer comprises drying chicken manure to obtain a moisture content of 40-50 %; mixing the dried chicken manure with an anaerobic ferment bacteria; anaerobic fermenting the mixture in a fermentation tank; adding a secondary anaerobic ferment bacteria in the fermentation tank; adding lysine and nitrogen, phosphorus, and potassium fertilizer obtained by mixing raw manure; drying to obtain a moisture content of 5-15 %; and adding zinc and selenium microelement.    USE - Method for the preparation of a fertilizer used for tea (claimed).    ADVANTAGE - The method is environment-friendly, and is inexpensive.
NOVELTY - An organic multi-element plant nutrition biopolymer comprises 50-80 pts. wt. crop straw, 10-30 pts. wt. livestock manure, 0.05-0.1 pt. wt. microbial agent, 5-10 pts. wt. coal cinder, 5-10 pts. wt. biological power plant ash, 2-4 pts. wt. bentonite, 0.1-0.2 pt. wt. nitrogen-fixing bacteria and 0.5-2 pts. wt. water retention agent. Biopolymer is manufactured by mixing straw and manure, inoculating with microbial agent, fermenting, turning at 60-70 degrees C, adding remaining raw materials, mixing, adjusting pH value to 6.5-7, and molding.    USE - Organic multi-element plant nutrition biopolymer for cultivating in non-agricultural land, i.e. saline land, desert, Gobi desert or city roof (claimed).    ADVANTAGE - The biopolymer is rich in phytonutrients, environment-friendly, and utilizes agricultural waste.
NOVELTY - A Taxodium cuttage substrate comprises organic fermentation material, peat, vermiculite and perlite at a mass ratio of 36-72:2:8-30:2-8. Organic fermentation material includes tea residue, rice chaff and mushroom residue at a mass ratio of 9-18:5:0.5-3.    USE - Taxodium cuttage substrate used for promoting root system development and increasing survival rate.    ADVANTAGE - The substrate is rich in organic matter, humic acid and various nutrients, labor-saving, resource-saving, and environment-friendly. Total savings can amount to 700-1000 Yuan/acre.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Taxodium cuttage substrate comprising mixing tea leaves, rice chaff and mushroom residue, stacking, adding 0.1-0.5 kg/m3 inoculating agents, fermenting, turning at 55-60 degrees C, transferring into fermentation tank, turning daily, fermenting for 8-10 days, adding remaining raw materials, and mixing.
NOVELTY - Avermectin granular insecticide and fertilizer comprises 0.005-0.015 kg avermectin raw powder, 32-36 kg of urea, 125-130 kg monoammonium phosphate, 65-68 pts. wt. potassium chloride, 0.3-0.5 kg Bacillus powder, 4-6 kg humic acid salt, 190-210 kg monosodium glutamate fermentation solution, 190-210 kg waste matter, 90-110 kg straw powder and 4260-4270 kg organic fertilizer. Fertilizer is prepared by taking all raw materials, stirring, drying, and granulating. Organic fertilizer is green manure, farmyard manure, human manure, compost, wet compost and/or biogas fertilizer.    USE - Avermectin granular insecticide and fertilizer for promoting plant growth, preventing and treating plant diseases, and eliminating insect pests.    ADVANTAGE - The fertilizer increases crop yield.    DETAILED DESCRIPTION - Avermectin granular insecticide and fertilizer comprises 0.005-0.015 kg avermectin raw powder, 32-36 kg of urea, 125-130 kg monoammonium phosphate, 65-68 pts. wt. potassium chloride, 0.3-0.5 kg Bacillus powder, 4-6 kg humic acid salt, 190-210 kg monosodium glutamate fermentation solution, 190-210 kg waste matter, 90-110 kg straw powder and 4260-4270 kg organic fertilizer. Fertilizer is prepared by taking all raw materials, stirring, drying at 45-50 degrees C for 0.5 hour, and granulating. Organic fertilizer is green manure, farmyard manure, human manure, compost, wet compost and/or biogas fertilizer. Avermectin raw powder, urea, monopotassium phosphate and potassium chloride purities are 95 wt.%, 46 wt.%, 48 wt.% and 60 wt.%, respectively. Bacillus powder contains 40 billion bacteria/g.
NOVELTY - Preparing marsh gas using straw, excrement and kitchen rubbish comprises (a) pretreatment: placing crushed straw, kitchen waste and manure into a pretreatment tank, mixing, placing in a pre-mixing tank, heating with constant temperature, and uniformly mixing to obtain mixture; and (b) placing the mixture into at least one anaerobic fermentation tank, heating with constant temperature, stirring, and fermenting to obtain marsh gas and fermentation residue.    USE - The method is useful for preparing marsh gas using straw, excrement and kitchen rubbish (claimed).    ADVANTAGE - The method: has stable operation and high efficiency; reduces the production cost; and is suitable for large-scale popularization.
NOVELTY - A sludge and then processing one's sewage treatment device, comprising an aerating tank (2), a sedimentation tank (4), a collecting cover (14) and (16), wherein the aeration tank (2) one end of the raw water inlet (1), and the other end of the pipe (3) is connected with the sedimentation tank (4) is connected with the aeration tank (2) is provided with a gas collecting device, said sedimentation tank (4)'s's bottom of the sludge return pipe (6), a mud reflowing pipe (6) is connected with the raw water inlet (1) is connected with the sludge return pipe (6) is set at the bottom's residual sludge discharge pipe (8), the residual sludge discharging pipe (8)'s lower part is set with mud tank (19), a mud tank (19) is connected with heating and dehydrating machine (20). The utility model has a blower device, which can ensure the enough oxygen aeration tank, a gas collecting device above the aeration tank, reduces the pollution to atmosphere,'s system's sludge to the heating and drying, convenient for subsequent processing.
NOVELTY - Production of organic liquid fertilizer comprises combusting rice hulls or bran at 200 degrees C in circular closed furnace, absorbing released flue gas, cooling into oily liquid under certain condition, and adding aqueous solution of 12 essential nutrients.    USE - Method for producing organic liquid fertilizer (claimed).    ADVANTAGE - The method is environment-friendly. The fertilizer is water-miscible and does not contain chemical hormone.
NOVELTY - Blueberry organic fertilizer is manufactured by performing alternate loose and tight stacking of fresh livestock manure in a composting site and providing enough ventilation on the stack.    USE - Method of manufacturing blueberry organic fertilizer (claimed).    ADVANTAGE - The method involves alternate loose and tight stacking of manure to shorten decomposition time and reduce nitrogen loss. The obtained organic fertilizer conforms to NY525-2002 Standard and has nitrogen-phosphorus-potassium total content of greater than or equal to 4%, organic matter content of greater than or equal to 30% and moisture content of less than or equal to 20%, and pH value of 5.5-8.
NOVELTY - Organic fertilizer is produced by adding lees and auxiliary material and uniformly mixing and stirring to obtain base material; adding fly maggot into base material and allowing to grow for 3-4 days to convert base material into protein-rich base material; separating the maggot, outdoor stacking the protein-rich base material and fermenting for 7-15 days to obtain organic fertilizer.    USE - Process of producing organic fertilizer (claimed).    ADVANTAGE - The process involves organic waste biological transformation using housefly larva, and has short fermentation period and high efficiency.
NOVELTY - Fertilizer raw material water content is controlled by connecting a top box of a fertilizer raw material water content regulator with an external power line, starting a motor to drive a screw rod and a top box to move upwards; filling stack material for composting containing excess water into bottom box at height of 60-70 cm; and starting motor to drive screw rod and top box to move downwards, continuously moving top box downwards, pressing stack material and draining excess water to bottom drain hole until required water content is achieved.    USE - Method of controlling fertilizer raw material water content (claimed).    ADVANTAGE - The method utilizes water content regulator which is simple and convenient to use and has simple structure and high strength.    DETAILED DESCRIPTION - Control of fertilizer raw material water content comprises:    (A) connecting top box of fertilizer raw material water content regulator with an external power line, starting a motor to rotate the motor and drive a screw rod and a top box to move upwards, when both sides of bottom box slider groove rise 50 cm, stopping the motor, and keeping top box position;    (B) filling stack material for composting containing excess water into bottom box at height of 60-70 cm; and    (C) starting motor to drive screw rod and top box to move downwards, inserting top box sliding rod with bottom box sliding groove, continuously moving top box downwards, pressing stack material and draining excess water to bottom drain hole until required water content is achieved.
NOVELTY - A fertilizer raw material water content regulator is manufactured by welding stainless steel plates to form two square shaped structures comprising bottom box and top box; providing central locating hole on middle of bottom box; fixing motor on middle part of top box, providing middle opening on the top box so that threaded rod passes through the middle opening, and connecting a motor output shaft with two side walls of top box; and buckling top box on the bottom box such that threaded rod passes through the central locating hole of the bottom box.    USE - Method of manufacturing fertilizer raw material water content regulator (claimed).    ADVANTAGE - The method is simple to operate and the obtained water content regulator product has simple structure and high strength and is convenient to use.    DETAILED DESCRIPTION - Manufacture of fertilizer raw material water content regulator comprises:    (A) welding stainless steel plates to form two square shaped structures comprising bottom box and top box;    (B) providing central locating hole on middle of bottom box, providing apertures around the locating hole, providing two side walls of bottom box with a slide rod groove, and welding bottom box support at two sides of bottom box end;    (C) fixing motor on middle part of top box, providing middle opening on the top box so that threaded rod passes through the middle opening, and connecting a motor output shaft with two side walls of top box; and    (D) buckling top box on the bottom box such that threaded rod passes through the central locating hole of the bottom box.
NOVELTY - A fertilizer raw material water content regulator comprises a support, a bottom box, and a top box. Center of the bottom box is provided with a locating hole. The locating hole is provided with parallel water drain holes. Two sides of bottom box upper wall are provided with a sliding groove. The sliding groove is fixed and welded on the bottom box.    USE - Fertilizer raw material water content regulator.    ADVANTAGE - The water content regulator has simple structure and high strength and is convenient to use.
NOVELTY - A biological organic fertilizer is prepared by mixing Pleurotus eryngii fungi residues, phosphoric acid, manganese chloride and water at a weight ratio of 80-200:50-200:5-25;600-800; stirring the mixture at 120-150 degrees C for 0.5-125 hours; neutralizing until the pH value is 6.6-7.2; filtering; adding nutrition material to the filtrate; mixing; adding natural source material; and mixing.    USE - Method of preparing a biological organic fertilizer (claimed).    ADVANTAGE - The method prepares product that improves soil, crop quality and yield.    DETAILED DESCRIPTION - A biological organic fertilizer is prepared by mixing Pleurotus eryngii fungi residues, phosphoric acid, manganese chloride and water at a weight ratio of 80-200:50-200:5-25;600-800; stirring the mixture at 120-150 degrees C for 0.5-125 hours; neutralizing until the pH value is 6.6-7.2; filtering; adding nutrition material to the filtrate; mixing; adding natural source material; mixing; adding 0.2-10 pts. wt. Bacillus subtilis having viable count of 5000000000 U/g, 0.2-10 pts. wt. yeast having viable count of 5000000000 U/g, 0.2-10 pts. wt. Trichoderma having viable count of 5000000000 U/g, 0-10 pts. wt. potassium containing bacteria having viable count of 5000000000 U/g, 0-10 pts. wt. phosphorus containing bacteria having viable count of 5000000000 U/g; mixing; adding 0.2-10 pts. wt. fertilizer additive; mixing; fermenting at 25-35 degrees C for 2-10 days. The nutrition material comprises 5-50 pts. wt. wheat bran, 5-50 pts. wt. rice bran, 0-20 pts. wt. brown sugar, 0-10 pts. wt. white sugar, and 0-10 pts. wt. glucose. The natural source material comprises 0-30 pts. wt. inorganic mineral rock phosphate, 0-50 pts. wt. potassium mineral powder, 0-30 pts. wt. plant ash, 0-5 pts. wt. borax, 0-20 pts. wt. magnesium ore powder by weight, 0-10 pts. wt. sulfur, and 0-5 pts. wt. gypsum or lime stone.
NOVELTY - A biofertilizer from farmland waste is prepared by mixing farmland waste, auxiliary material and vermiculite at volume ratio of 2:1:1, adding modified Melin-Norkrans liquid culture medium, mixing, cultivating at 25 degrees C for 15 days, inoculating with ectomycorrhizal fungi, taking mycelium, and mixing 25 vol.% fermented biomass, 15 vol.% biological activated carbon, 5 vol.% water retention agent and 1 vol.% biological activity promoting component.    USE - Method for preparing biofertilizer from farmland waste (claimed) for promoting root system development and seedling growth, strengthening drought and salt resistance, and improving photosynthesis.    ADVANTAGE - The fertilizer improves nutrient absorption, activates beneficial soil microorganisms, and improves plant quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for 3 application methods of biofertilizer comprising:    (A) direct application by trenching, exposing roots, adding 150 g/2.5 cm fertilizer, mixing with soil, earthing, and watering;    (B) liquid application by trenching, exposing roots, diluting 1 kg fertilizer with 30-40 kg water, stirring, and pouring 1 L/2.5 cm solution; and    (C) soil matrix by administering 3 g/L fertilizer in spring and autumn.
NOVELTY - A soil conditioner comprises 55-60 wt.% bagasse, 15-25 wt.% straw, 10-15 wt.% soybean meal, 5-10 wt.% humic acid fertilizer and 0.5-2 wt.% mixed microbial inoculum.    USE - Soil conditioner used for improving soil fertility.    ADVANTAGE - The method is simple, environment-friendly and low-cost. The soil conditioner improves soil physical and chemical structure, eliminates soil hardening and balances soil pH.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soil conditioner comprising taking raw materials, adjusting moisture content to 60-70%, placing in fermenter, adjusting pH to 6.0-7.0, heating to 70 degrees C for 1-2 days, fermenting at 70 degrees C for 1-3 days, cooling to about 40 degrees C for 4-6 days, and drying at less than or equal to 70 degrees C.
NOVELTY - Continuous multistep synthesis of 2,3,3,3-tetrafluoropropene comprises mixing hydrogen and hexafluoropropylene at molar ratio of 3-20:1, hydrogenating in presence of hydrogenation catalyst at 30-250 degrees C with space velocity of 500-5000 per hour, adding alkali and organic solvent at a mass ratio of 1-50:1, performing dehydrofluorination at 50-150 degrees C, condensing, hydrogenating at 80-250 degrees C, adding alkali and organic solvent, and reacting at 50-150 degrees C, and condensing. Working pressure is atmospheric pressure to 1 MPa.    USE - Method for continuously synthesizing 2,3,3,3-tetrafluoropropene (claimed).    ADVANTAGE - The synthesis has simple technique, low equipment investment, low energy consumption, and less waste generation.
NOVELTY - Environment-friendly catalytic oxidation of glutaraldehyde to prepare adipaldehyde comprises providing phosphotungstic acid, supported phosphotungstic acid, or composite tungsten oxide as catalyst and 10-70 wt.% aqueous hydrogen peroxide solution as oxidant, and conducting catalytic oxidation of glutaraldehyde at 40-95 degrees C for 4-24 hours, where molar ratio of hydrogen peroxide and glutaraldehyde is 2.0-4.0 and the amount of catalyst is 1-4 mol.% of the amount of glutaraldehyde.    USE - Environment-friendly catalytic oxidation of glutaraldehyde to prepare adipaldehyde (claimed).    ADVANTAGE - The method has mild condition, simple technique, low cost, high yield i.e. 95-99%, purity of greater than or equal to 99.0%, and solvent-free reaction system and is environment-friendly.
NOVELTY - An optically active amlodipine is prepared by dissolving racemic amlodipine and (S)-(-)- alpha -methylbenzyl isocyanate in acetone, reacting to generate (S)-(-)-amlodipine (S)-(-)- alpha -isocyanate, filtering, adding ethanol, and neutralizing by sodium hydroxide.    USE - Preparation of optically active amlodipine (claimed).    ADVANTAGE - Preparation process is easy, non-toxic, can be recycled, and environment-friendly.
NOVELTY - A clevidipine butyrate is prepared by mixing (E)-2-(2, 3-dichlorine subbenzyl)-3 oxo-butyric acid and butyric acid methyl chloride in dichloromethane and/or acetone, adding alumina load inorganic alkali catalyst at 40-80 degrees C to generate 2, 3-dichlorobenzyl acetoacetate butyryl ester, mixing with 3-amino crotonic acid methyl ester in methanol and/or ethanol, and reflux heating.    USE - Preparation of clevidipine butyrate (claimed).    ADVANTAGE - Preparation process improves reaction atoms utilization rate, avoids traditional toxic synthesis method and poisonous catalyst, increases industrial synthesis cleanness, and reduces environmental pollution.
NOVELTY - A 5-((1S)-2-cyclopropyl-1-(2-fluorophenyl)-2-oxoethyl)-4,5,6,7-tetrahydrothieno(3,2-c)pyridin-2-yl acetate hydrobromide acetic acid salt is new.    USE - A new 5-((1S)-2-cyclopropyl-1-(2-fluorophenyl)-2-oxoethyl)-4,5,6,7-tetrahydrothieno(3,2-c)pyridin-2-yl acetate hydrobromide acetic acid salt (claimed).    ADVANTAGE - The salt compound is easy to prepare and has high level of purity.    DETAILED DESCRIPTION - A 5-((1S)-2-cyclopropyl-1-(2-fluorophenyl)-2-oxoethyl)-4,5,6,7-tetrahydrothieno(3,2-c)pyridin-2-yl acetate hydrobromide acetic acid salt (C22H25FNO5SBr) of formula (I) is new. An INDEPENDENT CLAIM is included for preparation of salt compound..
NOVELTY - Cefuroxime is prepared by mixing purified water, 7-aminocephalosporanic acid and sodium hydroxide solution, cooling at 0-15 degrees C, separately mixing phosphorus pentachloride with methylene dichloride, adding 2,2-furan ammonium acetate , heating at 20-30 degrees C for 0.5-2 hours to obtain acyl chloride mixture, mixing acyl chloride mixture with 7-aminocephalosporanic acid-sodium hydroxide mixture at 15-25 degrees C to induce condensation reaction, standing to allow layers to divide, separating aqueous phase, adding ethanol and hydrochloric acid, stirring to induce crystallization, and filtering.    USE - Preparation of cefuroxime (claimed).    ADVANTAGE - The preparation scheme is fast, uses non-toxic raw materials, and involves mild reaction conditions.    DETAILED DESCRIPTION - Cefuroxime is prepared by mixing purified water, 7-aminocephalosporanic acid (7-ACA) and sodium hydroxide solution in which mass ratio 7-ACA:purified water is 1:2-4, cooling at 0-15 degrees C until 7-aminocephalosporanic acid is completely dissolved, separately mixing phosphorus pentachloride with methylene dichloride, adding 2,2-furan ammonium acetate in which mass ratio phosphorus pentachloride:2,2-furan ammonium acetate is 0.5-0.7:1 and mass ratio 2,2-furan ammonium acetate:7-aminocephalosporanic acid is 0.6-0.8:1, heating at 20-30 degrees C for 0.5-2 hours to obtain acyl chloride mixture, mixing acyl chloride mixture with 7-ACA-sodium hydroxide mixture at 15-25 degrees C to induce condensation reaction, standing to allow layers to divide, separating aqueous phase, adding ethanol and hydrochloric acid, stirring to induce crystallization, and filtering.
NOVELTY - Processing of solid organic waste involves introducing the solid organic waste into a pyrolysis furnace, and producing a pyrolysis gas.    USE - Processing of solid organic waste (claimed).    ADVANTAGE - The method enables the processing of solid organic waste with the gas having high calorific value.
NOVELTY - A Pseudomonas fluorescens strain Y13 (CCTCC M2012121), is new.    USE - The P.fluorescens is useful for dissolving phosphorus in soil and increasing phosphorus and phosphorus in soil (all claimed).    ADVANTAGE - The P.fluorescens can be obtained easily and cost-effectively, enables plants to provide high-yield, reduces the planting cost, and relieving the excess agricultural fertilizer application which causes environment pollution.
NOVELTY - A Paenibacillus sp. 18WLY (CGMCC NO: 7724), is new.    USE - The Paenibacillus sp. 18WLY is useful for preparing genetically engineered E.coli strain 78-7 which is useful in microbial inoculum or bio-organic fertilizer for fixing biological nitrogen (all claimed). The nitrogen fixation gene cluster is useful for preparing transgenic crop capable to fix nitrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) nitrogen fixation gene cluster; (2) expression vector; (3) host cell or host bacteria; (4) method for constructing the genetically engineered Escherichia coli strain 78-7; and (5) genetically engineered E.coli strain 78-7.
NOVELTY - Method for producing microbial inoculum for garbage, involves performing liquid fermentation of Bacillus cereus, Lactobacillus acidophilus, B.stearothermophilus, Pseudomonas pseudoalcaligenes and Saccharomyces cerevisiae, performing spray-drying method of microorganism, weighing B.cereus, L.acidophilus, B.stearothermophilus, P.pseudoalcaligenes and S.cerevisiae, and uniformly mixing microorganism, and mixing dried powder with obtained microorganism.    USE - The method is useful for producing microbial inoculum for processing garbage (all claimed).    ADVANTAGE - The method is simple.    DETAILED DESCRIPTION - Method for producing microbial inoculum for garbage, involves (a) performing liquid fermentation of Bacillus cereus, Lactobacillus acidophilus, B.stearothermophilus, Pseudomonas pseudoalcaligenes and Saccharomyces cerevisiae, (b) performing spray-drying method of microorganism to obtain super-concentrated microorganism powder having spore content of 109-1010 colony-forming unit (cfu)/g, (c) weighing 30-100 pts. wt. B.cereus, 100-300 pts. wt. L.acidophilus, 100-150 pts. wt. B.stearothermophilus, 50-120 pts. wt. P.pseudoalcaligenes and 80-150 pts. wt. S.cerevisiae, and uniformly mixing microorganism, and (d) mixing dried powder with obtained microorganism.
NOVELTY - Production of natural amino acid involves collecting slaughter animal blood in a slaughtering device, adding 0.1-0.2% lipase, stirring uniformly for 1-3 hours, fermenting, decomposing fat in the blood, adding 0.1-0.5% proteases, stirring uniformly, fermenting, decomposing protein in the blood, adding 1-5% acetic acid solution, stirring uniformly, filtering, carrying out ultraviolet sterilizing treatment, performing solid-liquid separation of the resultant solution, obtaining liquid amino acid material and slurry solid material, discharging the liquid amino acid material, and storing.    USE - Production of natural amino acid used for fertilizer (claimed).    ADVANTAGE - The method efficiently and economically provides natural amino acid, by a simple process.    DETAILED DESCRIPTION - Production of natural amino acid involves collecting slaughter animal blood in a slaughtering device, adding 0.1-0.2% lipase, stirring uniformly, fermenting for 1-2 hours, decomposing fat in the blood, adding 0.1-0.5% proteases, stirring uniformly for 1-3 hours, fermenting, decomposing protein in the blood, adding 1-5% acetic acid solution, stirring uniformly for 10 minutes, filtering through filtering device to remove impurities, carrying out ultraviolet sterilizing treatment in an ultraviolet sterilizing device, performing solid-liquid separation of the resultant solution in a separation device, obtaining liquid amino acid material and slurry solid material, discharging the obtained liquid amino acid material, and storing in liquid material storage device at low temperature of 0-7 degrees C. An INDEPENDENT CLAIM is included for usage of natural amino acid.
NOVELTY - Formulation comprises a mixture of active substance of a compound including 3-(4-cinnamyl-1-piperazinyl)-amino derivatives of 3-formylrifamycin SV and 3-formylrifamycin S and their excipients, where the excipients are present in an amount of 1-25 wt.%.    USE - The formulation is useful for prophylaxis and treatment of diseases caused by gram-positive, gram-negative microorganisms, and tuberculous mycobacteria. No biological data given.    ADVANTAGE - The readily feasible formulation can be economically prepared using environmental friendly solvents with high yield, purity and biological activity and reduced time consumption and without requiring additional equipment for its implementation, exhibits good solubility in water, faster resorption and better pharmacokinetic properties in in vivo experiments, and treats bacterial disease with reduced toxicity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing 3-(4-cinnamyl-1-piperazinyl)-iminomethyl rifamycin SV comprising reacting 3-formylrifamycin SV with an ethanol solution of N1-cinnamyl-N4-aminopiperazin in the presence of small amounts of acetic acid at 20-30 degrees C, additionally adding 3-formylrifamycin SV to obtained reaction mixture, diluting the reaction mixture with equal volume of water, filtering the mixture to obtain a precipitate, and washing the precipitate with water;    (2) preparing a sodium salt of the compound comprising reacting the 3-(4-cinnamyl-1-piperazinyl) iminomethyl rifamycin SV with an equimolar amount of sodium methoxide in ethanol, at 20-30 degrees C, distilling off the ethanol, dissolving obtained residue in water in the presence of sodium ascorbate, and lyophilizing obtained aqueous solution; and    (3) a phenol derivative of formulae (I) and (II).    R = H or Na; and    R1 = COCH3 or H.
NOVELTY - Preparing a pyrazole carboxylic acid derivative (I), comprises (a) reacting an oxoacetate (II) with an acrylate (III) in the presence of a base to form an aminomethylene succinic acid ester (IV), (b) coupling (IV) with an N-protected hydrazine derivative (V) to form hydrazinomethylene succinic acid ester (VI), (c) ring closing (VI) under acidic conditions to form pyrazole dicarboxylic acid ester (VII), and (d) hydrolyzing (VII) in 3-position with a base to form (I).    USE - The process is useful for preparing (I) (claimed), which is useful as building block in the preparation of active compounds for treating psychotic disorders including schizophrenia. No biological data given.    ADVANTAGE - The process is capable of economically preparing (I) with high selectivity and purity in an industrial and eco-friendly manner.    DETAILED DESCRIPTION - Preparing a pyrazole carboxylic acid derivative of formula (I), comprises (a) reacting an oxoacetate of formula (II) with an acrylate of formula (III) in the presence of a base to form an aminomethylene succinic acid ester of formula (IV), (b) coupling (IV) with an N-protected hydrazine derivative of formula (V) to form hydrazinomethylene succinic acid ester of formula (VI), (c) ring closing (VI) under acidic conditions to form pyrazole dicarboxylic acid ester of formula (VII), and (d) hydrolyzing (VII) in 3-position with a base to form (I).;    R1 = 1-7C-alkyl;    R3 = 1-7C-alkyl (optionally substituted with halo or 1-4C-alkoxy);    R2 = 1-7C-alkyl;    X = halo;    R4, R5 = 1-7C-alkyl; and    R6 = amino protecting group comprising tert-butoxycarbonyl (Boc), fluorenylmethoxycarbonyl (Fmoc), benzyloxycarbonyl (Cbz), p-methoxybenzyl carbonyl (Moz), acetyl or formyl.    An INDEPENDENT CLAIM is included for hydrazinomethylene succinic acid ester (VI).
NOVELTY - Stack of industries biodegradable material, beverages and other foods biodegradation involves utilizing vermicompost.    USE - Method for biodegrading stack of industrial biodegradable sludge, beverages, and other foods to obtain product used in agriculture area to mitigate pollution of water bodies by managing chemical oxygen demand, biochemical oxygen demand, phosphorus content and nitrogen content (all claimed).
NOVELTY - Extraction of oryzanol from rice bran crude oil comprises stirring 4-5 times ether non-polar solvent and 2 times polar alcohol solvent to rice bran crude oil, diluting, adjusting pH to 10 by sodium hydroxide, standing to divide into layers, separating lower layer, extracting with ether non-polar solvent, adjusting pH to 7, vaporizing and recycling solvent to obtain crude product, and bleaching and refining crude product.    USE - Method for extracting oryzanol from rice bran crude oil (claimed).    ADVANTAGE - The economical method having high yield avoids oil loss and environmental pollution, and saves production cost.
NOVELTY - Bio-fertilizer comprises 0.01-0.02 wt.% deodorant composting agent, 4-6 wt.% humic acid, 0.1-0.2 wt.% effective microorganisms (EM) composition, 0.1-0.2 wt.% sugar, 0.005-0.01 wt.% trace elements and remainder base material. The EM composition comprises photosynthetic bacteria, lactic acid bacteria, yeast, Gram-bacteria in soil and crop, and other beneficial micro flora. The base material is one or more chosen from animal excrement, domestic garbage, straw, rice bran and wheat bran powder.    USE - As bio-fertilizer.    ADVANTAGE - The fertilizer is environmentally-friendly and reduces waste material, thus is prevents pollution and protects environment.    DETAILED DESCRIPTION - Bio-fertilizer comprises 0.01-0.02 wt.% deodorant composting agent, 4-6 wt.% humic acid, 0.1-0.2 wt.% effective microorganisms (EM) composition, 0.1-0.2 wt.% sugar, 0.005-0.01 wt.% trace elements and remainder base material. The EM composition comprises photosynthetic bacteria, lactic acid bacteria, yeast, Gram-bacteria in soil and crop, and other beneficial micro flora. The base material is one or more chosen from animal excrement, domestic garbage, straw, rice bran and wheat bran powder. The humic acid increases the composting of organic matter and adjusts pH of the compost. An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) selecting open production sites, (b) stacking the base material in cross section in strip-shaped ladder formation, where the width and height of the ladder in a ratio of 2-2.5:1, (c) sprinkling the humic acid uniformly on the stacked material, (d) adding deodorant composting agent, mixing uniformly and crushing the mixture, and performing aerobic fermentation by supplying oxygen, (e) adding trace elements and mixing uniformly, (f) mixing EM composition and sugar, and diluting in water and adding the diluted solution, (g) closing the strips of the stack for fermentation, and (h) obtaining the product.
NOVELTY - Recycling Eupatorium adenophorum comprises dividing E. adenophorum into wood raw material and grass raw material; crushing grass raw material into powder, adding Rw decay accelerating agent, mixing uniformly, adding water till water content is 55-60%, controlling temperature, and fermenting; crushing wood raw material, carbonizing, cooling, and crushing; and mixing compost and carbonized material, where ratio is 1:3-5, adding 5-10 wt.% adhesive, and pressing in granulator.    USE - Method for recycling Eupatorium adenophorum (claimed) used as fertilizer and for mining wasteland vegetation restoration.    ADVANTAGE - The recycled Eupatorium adenophorum has fertilizer function, retains water, keeps temperature, has slow-release effect, and improves soil.
NOVELTY - Agricultural organic fertilizer is prepared by mixing pig manure and straw, fermenting the mixture, drying the fermented mixture, and mixing the dried product with fly ash.    USE - The agricultural organic fertilizer is useful for vegetables.    ADVANTAGE - The agricultural organic fertilizer is cost-effective, and improves yield of vegetables.
NOVELTY - Converting pig manure into solid soil culture, by (a) paving cushion material on the cement ground, (b) breeding density region of pig, (c) providing fermentation and feeding area corresponding to same area of the sawdust, and mixing pig manure thoroughly to form aqueous fermentation mixture, and (d) fermenting mixture under aerobic microorganisms by mixing sawdust and pig manure, maintaining fermentation mixture, ripening the mixture, fermenting ripened mixture by piling, and decomposing to form a solid soil culture.    USE - The method is useful for converting pig manure into solid soil culture (claimed).    ADVANTAGE - The method is simple, easy to operate, and flexible, consumes low energy, solves pig breeding pollution, improves benefit of pig breeding, obtains resource utilization, and realizes ecological agriculture.    DETAILED DESCRIPTION - Converting pig manure into solid soil culture, involves (a) paving cushion material on the cement ground, where pad material is composed of sawdust, cement ground is provided with 140-152 kg/m2, and sawdust piled into window shape to height of 50-100 cm, (b) breeding density region of pig is 1-1.61 head/m2, (c) providing fermentation and feeding area corresponding to same area of the sawdust, and mixing pig manure thoroughly to form an 45-70% aqueous fermentation mixture, and (d) fermenting mixture under aerobic microorganisms for 20-30 days by mixing sawdust and pig manure, maintaining fermentation mixture temperature to 50 degrees C or more, ripening the mixture for 23 months, fermenting ripened mixture by piling at 50 degrees C, and decomposing to form a solid soil culture.
NOVELTY - Production of organic fertilizer comprises selecting raw materials comprising pig manure; drying and sterilizing; fermenting; semi-wet crushing; mixing with nitrogen, phosphorus and potassium; granulating; drying; sieving; packaging qualified product, while returning not qualified product into granulating step; sealing; and storing.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method has short production time, low energy consumption, and high drying efficiency and good deodorizing and fly-killing effect of fermentation product.
NOVELTY - A biological organic crop seedling stage high-yield nutrient fertilizer comprises 13-35 pts. wt. nitrogenous fertilizer, 20-50 pts. wt. phosphate fertilizer, 30-70 pts. wt. organic fertilizer, 1-5 pts. wt. biological microbial inoculum and 0.05-0.3 pt. wt. root-promoting powder. The nitrogenous fertilizer is ammonium nitrate and/or urea.    USE - Biological organic crop seedling stage high-yield nutrient fertilizer used for maize.    ADVANTAGE - The fertilizer has average yield of more than 8%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic crop seedling stage high-yield nutrient fertilizer comprising mixing traditional Chinese medicine slag and humic acid, adding cellulose-decomposing bacteria, fermenting for 10-20 days, mixing with other raw materials and pelletizing.
NOVELTY - A Stropharia rugosoannulata culturing material comprises 65-75 wt.% broad bean skin, 13-23 wt.% broadleaf tree wooden chips, 5 wt.% bacterial residue, 5 wt.% dairy manure, 1 wt.% gypsum powder and 1 wt.% lime powder.    USE - Stropharia rugosoannulata culturing material.    ADVANTAGE - The culturing material has reasonable proportion, balanced nutrition, good ventilation property, strong water-preserving property and high yield. It has biological efficiency of 112.8-125.4%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Stropharia rugosoannulata culturing material comprising drying raw materials for 1-2 days, killing bacteria by UV light, pre-wetting broad bean skin, broadleaf tree wooden chips, bacterial residue, dairy manure and gypsum powder with 1% aqueous lime solution, uniformly stirring, stacking, covering upper part with tarpaulin, naturally fermenting, turning when temperature reaches 60 degrees C, keeping for 24 hours, adding water and turning for 4-5 times for 6-7 days.
NOVELTY - A skin type drug is synthesized by reacting compounds under action of nickel catalyst.    USE - Synthesis of skin type drug involves (claimed).    ADVANTAGE - Synthesis process has short route, mild reaction, high product yield, and simple operation and is low-cost and environment-friendly.    DETAILED DESCRIPTION - A skin type drug is synthesized by reacting compound of formula (I) and compound of formula (II) under action of nickel catalyst and reacting with compound of formula (MeMgX).    X=Cl or Br;    Et=ethyl;    Ph=phenyl; and    Me=methyl.
NOVELTY - A chimanine D is prepared by crushing Galipea longiflora leaves into coarse powder, adding 70-95% ethanol solution with amount of 5-10 times of amount of powder, carrying out continuous countercurrent extraction with ultrasonic treatment for 20-100 minutes at 25-55 degrees C to obtain extracted solution, concentrating, adding alumina, drying column packing, eluting with chloroform-acetone mixture by thin layer chromatography, collecting chimanine D, concentrating, separating by preparative liquid chromatography with UV detector online detection, and collecting chimanine D.    USE - Preparation of chimanine D for pharmaceutical raw material.    ADVANTAGE - Preparation method is simple, has short reaction time and high product yield and purity, and recycles solvent.    DETAILED DESCRIPTION - A chimanine D is prepared by crushing Galipea longiflora leaves into coarse powder, adding 70-95% ethanol solution with amount of 5-10 times of amount of powder, carrying out continuous countercurrent extraction with ultrasonic treatment for 20-100 minutes at 25-55 degrees C to obtain extracted solution, concentrating, adding alumina, drying column packing, eluting with chloroform-acetone mixture by thin layer chromatography, collecting chimanine D, concentrating, separating by preparative liquid chromatography with UV detector online detection, collecting chimanine D, evaporating eluent in rotary evaporator to obtain chimanine D coarse particles, recrystallizing with chloroform-acetone mixture, freezing, and drying.
NOVELTY - A natural mineral fertilizer comprises 35-55% silkworm, 8-37% urea, 5-17% potassium dihydrogen phosphate, 20-45% attapulgite powder, and 5-10% humic acid.    USE - A natural mineral fertilizer.    ADVANTAGE - The fertilizer improves the ability to resist disease, improves stability of chemical fertilizer utilization rate, reduces agricultural production cost, improves product quality and yield, improves soil and protects ecological environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of natural mineral fertilizer comprising mixing urea, potassium dihydrogen phosphate, attapulgite powder, and humic acid in water to prepare nutrient solution, and spraying the dry decomposed silkworm dropping, where the water content of the silkworm dropping is reduced to 15-20%.
NOVELTY - A vegetable cultivation substrate comprises 10-20 wt.% peat, 10-20 wt.% perlite, 10-15 wt.% vermiculite, 0.3 wt.% potassium sulfate compound fertilizer, 5 wt.% rotten sheep manure, and forest waste branch.    USE - A vegetable cultivation substrate.    ADVANTAGE - The vegetable cultivation substrate is inexpensive, is environment-friendly, and has improved nutrient balance, thus improving vegetable growth and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermenting the forest waste branch, comprising crushing tree branches into grain diameter of not greater than 8 mm particles, adding fresh chicken manure for adjusting carbon to nitrogen ratio at 30/1-35/1, adding 0.1-0.5 wt.% fermentation microbial inoculum, adding water to adjust moisture content at 55-60%, uniformly mixing until stack temperature is increased to 50 degrees C, keeping the stack temperature for greater than or equal to 20 days at 55-65 degrees C, and turning once every 2 days until the stack temperature is reduced to below 30 degrees C and the moisture content is 20-30%.
NOVELTY - Preparation of quinolinone alkaloid (I), involves culturing Aspergillus (HM 991281) in culture medium, fermenting Aspergillus (HM 991281) using fermentation medium, filtering resulting fermentation broth, removing residues, concentrating filtrate, extracting the filtrate using ethyl acetate, concentrating extract under reduced pressure, performing chromatography, and concentrating resulting eluate to obtain a colorless oil.    USE - The method is useful for preparation of quinolinone alkaloid for controlling fouling odor of Balanus amphitrite larvae settled at bottom of marine (claimed).    ADVANTAGE - The method is suitable for large scale production, and environmentally-friendly.    DETAILED DESCRIPTION - Preparation of quinolinone alkaloid of formula (I), involves culturing Aspergillus (HM 991281) in culture medium, fermenting Aspergillus (HM 991281) using fermentation medium, filtering resulting fermentation broth, removing residues, concentrating filtrate, extracting the filtrate using ethyl acetate, concentrating extract under reduced pressure, performing chromatography, and concentrating resulting eluate to obtain a colorless oil.
NOVELTY - Preparation of chitin biological culture medium comprises adding processed 4000 pts. wt. crab shell and 6000 pts. wt. shrimp shell in a reaction kettle, and adding 5 pts. wt. Bacillus pumilus, 95000 pts. wt. water, and 5000 pts. wt. glacial acetic acid solution at 45 degrees C for 3 hours; treating 100 pts. wt. crab shell and shrimp shell mixture by adding 1000 pts. wt. hydrochloric acid solution at 60 degrees C for 1 hour; mixing 10 pts. wt. crab shell and shrimp shell, oven-drying at 85 degrees C for 30 minutes; crushing to 50-60 meshes; and mixing with 10 pts. wt. sand and 2 pts. wt. white diatomite.    USE - Method for the preparation of chitin biological culture medium used as an organic fertilizer (claimed).    ADVANTAGE - The method provides high quality chitin biological culture medium. The fertilizer improves soil environment.    DETAILED DESCRIPTION - Preparation of chitin biological culture medium comprises degreasing, manual rolling of crab and fat removing shrimp shell, after the crab shell and shrimp shell, desalting at 85 degrees C in hot water for 25 minutes, and drying until moisture content of chitin is 5%; adding 4000 pts. wt. crab shell and 6000 pts. wt. shrimp shell in a reaction kettle, and adding 5 pts. wt. B. pumilus, 95000 pts. wt. water, and 5000 pts. wt. of 5% glacial acetic acid solution at a constant temperature of 45 degrees C for 3 hours; treating 100 pts. wt. crab shell and shrimp shell mixture by adding 1000 pts. wt. of 2% of hydrochloric acid solution at a constant temperature of 60 degrees C for 1 hour; mixing the treated 10 pts. wt. crab shell and shrimp shell, oven-drying at 85 degrees C for 30 minutes under sterilization; crushing dried crab shell and shrimp shell to 50-60 meshes; and stirring and mixing with 10 pts. wt. of 40 meshes sand and 2 pts. wt. white diatomite.
NOVELTY - A culturing material comprises 20-30 wt.% chestnut tree meal, 18-22 wt.% corn meal, 12-18 wt.% oak chip, 20 wt.% cottonseed hull, 12 wt.% bran, 5 wt.% corn powder, 1 wt.% gypsum powder, and 2 wt.% lime powder.    USE - Culturing material used for Hypsizigus marmoreus (claimed).    ADVANTAGE - The material has biological efficiency of 103.7-112.5% and reduces cost of production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation culturing material comprising exposing raw material to UV for l-2 days for ultraviolet killing of bacteria; dry mixing chestnut tree meal, corn meal, and oak chip, uniformly stirring, prewetting with 2% lime water solution, piling wet material at a height of 1.0-1.2 m and width of 2-3 m, controlling weight of each stack at 300-500 kg, inserting stick having a diameter of 10-15 cm to make vertical air holes through the stack, covering upper part with tarpaulin for natural fermentation, turning, keeping temperature at 60 degrees C for 24 hours, turning stack once every after a day, on the third turning adding cottonseed hull, bran, corn powder, gypsum powder and auxiliary material, adding water, turning for 4-5 times for 6-7 days, stopping fermentation, maintaining water content at 63-65%; transferring 1100-1200 g wet material into each 17 cmx 35 cmx 0.005 cm polypropylene plastic bag, covering; sterilizing at normal pressure, discharging cooling gas when temperature reaches 100 degrees C, keeping for 8-10 hours, and naturally cooling to less than 25 degrees C.
NOVELTY - A Trichoderma asperellum strain 12 (CCTCC NO: M 2013213) capable of preventing and controlling rice sheath blight, is new.    USE - The T.asperellum strain 12 is useful for preventing and controlling rice sheath blight (claimed).    ADVANTAGE - The strain provides prevention rate of 70%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing bioorganic fertilizer, which involves inoculating T.asperellum strain into potato dextrose agar (PDA) culture medium, adding rice husk, straw and manure in a ratio of 50:30:20, and performing solid fermentation.
NOVELTY - The apparatus comprises first and second reaction tanks for organic waste being stirred, a compressor that provides air under high pressure and is connected to an air aeration pipe, a driver for driving multiple blades and a mixing part within the reaction tanks, and an air supply portion for supplying the air to a blower through an air supply pipe. The air aeration pipe is provided within a bottom surface of the reaction tanks. An inner side of the air supply pipe is arranged in the reaction tanks through a supply hole. The reaction tank controls humidity of the water jetted through a pump.    USE - The apparatus is useful for treating organic waste (claimed).    ADVANTAGE - The apparatus has improved fermentation capacity.    DETAILED DESCRIPTION - The apparatus comprises first and second reaction tanks for organic waste being stirred, a compressor that provides air under high pressure and is connected to an air aeration pipe, a driver for driving multiple blades and a mixing part within the reaction tanks, and an air supply portion for supplying the air to a blower through an air supply pipe. The air aeration pipe is provided within a bottom surface of the reaction tanks. An inner side of the air supply pipe is arranged in the reaction tanks through a supply hole. The reaction tank controls humidity of the water jetted through a pump. The pump is connected to a water pipe arranged on the first reaction tank. A hydrometer is fixed in one side of the reaction tanks. Other side of the reaction tanks is segmented with a partition wall. An exhausting unit is placed in the reaction tanks, and passes air through an anion deodorizing device. The exhausting unit includes a water tub, and an exhaust pipe. The exhaust pipe is configured for removing dust from the water tub. The water tub is positioned at end of the anion deodorizing device. The exhaust pipe is extended in the anion deodorizing device, and is arranged outside of the reaction tanks.
NOVELTY - Preparation (p1) of organic manure involves: (a1) homogenously mixing curd and jaggery; (b1) fermenting the curd and jaggery till a foul smell start coming, to obtain a fermented product; (c1) diluting the fermented product with water; (d1) mixing fly ash and cow dung to produce a manure mixture; (e1) dumping the manure mixture into an aerobic tank; (f1) pouring fermented product in aerobic tank, followed by diluting with water; and (g1) collecting organic manure after the foul smell disappears.    USE - For the preparation of organic manure (claimed) which are natural products used by farmers to provide food (plant nutrients) for the crop plants.    ADVANTAGE - The present method is cost-effective, quick and convenient; is easy process for the preparation of organic manure with easily available raw materials; has easy maintenance; does not harmful to humans; and is used as extra source of phosphorus, calcium, magnesium, and other elements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic manure prepared by the method (p1).
NOVELTY - Manufacturing organic liquid fertilizer, comprises mixing nitrogen and carbon source in different proportions respectively, preparing fermentation broths of different composition with fertilizing efficiency by adding microorganism to the above obtained mixture respectively and then fermenting, and adjusting the composition by mixing the fermentation broths of different composition.    USE - The method is useful for manufacturing organic liquid fertilizer (claimed).    ADVANTAGE - The organic liquid fertilizer is environmentally friendly (claimed), contains organic and inorganic substances necessary for plant growth, and is manufactured by using agriculture, livestock, and fishery by-products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the organic liquid fertilizer manufactured by the above method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for manufacturing organic liquid fertilizer (Drawing includes non-English language text).
NOVELTY - Treating livestock wastewater, comprises (i) inflowing livestock wastewater into an aeration tank in the presence of air, (ii) performing primary culturing on the obtained livestock wastewater using mixotrophic microalgae, and performing secondary culturing with beneficial microorganisms, (iii) precipitating undissolved materials by allowing to stand microalgae and microorganism, (iv) separating supernatant from livestock wastewater precipitate, and culturing supernatant with nutrition required microalgae.    USE - The method is useful for treating livestock wastewater (claimed).    ADVANTAGE - The method solves the problems of long-term treatment period and pre-treatment process for solid-liquid separation demand; utilizes two types of dominant photosynthetic microalgae, which processes livestock wastewater without pre-treatment process; adjusts the growth of microalgae in the wastewater under optimal conditions and remove organic matter and nutrients in the wastewater; decomposes the substances that causes high turbidity and eutrophication of river using carbon dioxide and light as energy source; is environmentally friendly; and reduces the livestock production costs by minimizing installation and wastewater treatment costs.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic flow chart of the method for treating livestock wastewater (Drawing includes non-English language text).    Livestock wastewater inflowing step (1)    Wastewater stabilizing step (2)    Secondary culturing step (3)    Precipitating step (4)    Tertiary culturing step (5)
NOVELTY - Preparing acid addition salts of (2-n-butyl-3-(4-(3-di-n-butylamino-propoxy) benzoyl)-5-methylsulfonamido benzofuran) (dronedarone) (I) comprises (a) O-alkylation of 2-n-butyl-3-(4-hydroxy benzoyl) 5-nitro benzofuran with 1-chloro-3-di-n-butylamino propane, (b) in-situ reduction of 2-n-butyl 3-(4-(3-di-n-butylamino-propoxy) benzoyl) 5-nitrobenzofuran, (c) mesylation of 5-amino 3-(4-(3-di-n-butylamino-propoxy)benzoyl)2-n-butyl benzofuran, and (d) conversion of dronedarone free base of 3-(4-(3-di-n-butylamino-propoxy)-benzoyl)-5-methyl-sulfonamide benzofuran into its acid addition salts of (I).    USE - The process is useful for preparing acid addition salts of (I) (claimed).    ADVANTAGE - The simple and improved process provides acid addition salts of dronedarone with high throughput, purity and degree of consistency and reproducibility and without using any hazardous chemicals in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - Preparing acid addition salts of (2-n-butyl-3-(4-(3-di-n-butylamino-propoxy) benzoyl)-5-methylsulfonamido benzofuran) (dronedarone) (I) comprises (a) O-alkylation of 2-n-butyl-3-(4-hydroxy benzoyl) 5-nitro benzofuran (II) with 1-chIoro-3-di-n-butylamino propane (III) in presence of inorganic base and phase transfer catalyst in a water immiscible organic solvent to get 2-n-butyl 3-(4-(3-di-n-butylamino-propoxy) benzoyl) 5-nitrobenzofuran (IV), (b) in-situ reduction of (IV) using heterogeneous metal catalyst under hydrogen pressure to get 5-amino 3-(4-(3-di-n-butylamino-propoxy)benzoyl)2-n-butyl benzofuran (V), (c) in-situ mesylation of (V) using mesyl chloride in presence of an inorganic base to obtain 3-(4-(3-di-n-butylamino-propoxy)-benzoyl)-5-methyl-sulfonamide benzofuran (VI), (d) in-situ conversion of dronedarone free base of (VI) into its acid addition salts of (I), by treating (VI) with acids, and (e) purification of the obtained acid addition salts of (I).
NOVELTY - Manufacturing amino acid fertilizer composition by using marine by-products, comprises (i) crushing fish skin product to obtain fish skin powder, (ii) performing alkaline extraction on the obtained fish skin powder to obtain alkaline removal solution containing proteins, (iii) performing alkaline hydrolysis on alkaline removal solution to obtain amino acid salt solution, (iv) neutralizing the amino acid salt solution to obtain amino acid liquid fertilizer, and (v) adding microelement in amino acid liquid fertilizer.    USE - The method is useful for amino acid fertilizer composition by using marine by-products (claimed).    ADVANTAGE - The method utilizes fish skin by-product, which does not generate zero emissions and economically produces amino acid rich fertilizer composition, and polymeric collagen and low molecular weight collagen peptide.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the method for manufacturing amino acid fertilizer composition by using marine by-products (Drawing includes non-English language text).
NOVELTY - A waste gas harmless processing system comprises waste gas inlet system (1), pressurized waste gas mixing system (3), catalytic processing system (6), waste gas detecting system (7) for detecting composition, conditioning system (9), air supply system (11), biochemical system (13), physical and chemical treatment system (15), liquid generating system (19), carrying liquid pipes (5, 8), high-temperature sterilizing system (21) and sludge dehydrating and drying system (17).    USE - Waste gas harmless processing system.    ADVANTAGE - The system has simple processing flow operation, simple structure and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of waste gas harmless processing system (Drawing includes non-English language text).    Waste gas inlet system (1)    Pressurized waste gas mixing system (3)    Carrying liquid pipes (5,8)    Catalytic processing system (6)    Waste gas detecting system (7)    Conditioning system (9)    Air supply system (11)    Biochemical system (13)    Physical and chemical treatment system (15)    Sludge dehydrating and drying system (17)    Liquid generating system (19)    High-temperature sterilizing system (21)
NOVELTY - Additive comprises 10-50 wt.% polysaccharide, 15-75 wt.% protein substances, and 0-15 wt.% fatty acid conjugate or nitrogen substances.    USE - The additive is useful for fermentation of biogas (claimed).    ADVANTAGE - The additive: ensures the fermentation of raw materials under anaerobic condition and rapidly introduces into glycolytic pathway; achieves continuous degradation and fast generation of biogas; and accelerates the pH of the feeding solution to neutral and improves the production rate.
NOVELTY - This utility model invention belongs to sewage processing technology field, claims a vacuum suction cleaning device from dynamic filter component with hollow fibre porous membrane. A dynamic base material composed of stainless steel screen, a filter cloth, a non-woven cloth, the water outlet direction of the water, the film base material is composed of a non-woven fabric, a filter cloth, a stainless steel silk screen, combined as a base material are symmetrically fixed on two sides of the plate-and-frame. , Plate-frame with cavity with a certain volume, is provided as a guide tube, an aeration system located at the bottom, a lifting surface. A bottom aeration, reverse water inlet and a seal suction device. A base material in a reactor containing active sludge of the trapped particles, strengthening function of biochemical reaction. This utility model is a component a base material has wide source, simple preparation, quick film hanging speed, stable standard short time, it can realize the film component of the online cleaning, and cleaning.
NOVELTY - The upflow anaerobic sludge blanket (UASB) device comprises an adjusting tank (2) and a UASB reaction tank (5). The adjusting tank is connected with a water inlet pipe. A bottom of the adjusting tank is provided with a layer of concentrated sludge. The concentrated sludge layer on a side of the adjusting tank is filled with sewage through the water inlet pipe. The adjusting tank is equipped with a stirrer on sides of an inner side wall. The adjusting tank is connected with the UASB reaction tank through an overflow pipe. The adjusting tank is provided with an air outlet.    USE - The UASB device is useful for treating sewage (claimed).    ADVANTAGE - The device improves biodegradability of wastewater, and increases chemical oxygen demand removal rate.    DETAILED DESCRIPTION - The upflow anaerobic sludge blanket (UASB) device comprises an adjusting tank (2) and a UASB reaction tank (5). The adjusting tank is connected with a water inlet pipe. A bottom of the adjusting tank is provided with a layer of concentrated sludge. The concentrated sludge layer on a side of the adjusting tank is filled with sewage through the water inlet pipe. The adjusting tank is equipped with a stirrer on sides of an inner side wall. The adjusting tank is connected with the UASB reaction tank through an overflow pipe. The adjusting tank is provided with an air outlet. The layer of concentrated sludge comprises acidifying bacteria. The adjusting tank comprises a methane pipe. An INDEPENDENT CLAIM is included for a method for treating sewage using a UASB device.
NOVELTY - Preparing an organic composition for bioremediation of polluted water comprises preparing the following components: 0.6-1% Aspergillus oryzae, 0.6-1% Bacillus cereus, 0.6-1% Aspergillus terreus, 0.6-1% Aspergillus nidulans, 50-60% hull, and water, mixing the components, and fermenting.    USE - The method is used for preparing an organic composition for bioremediation of polluted water (claimed). The composition is used to enhance the water quality.
NOVELTY - Producing carbon raw material comprises drying the carbon and then crushing and sieving into 10-100 meshes of fine powder, collecting the mud carbon and then adding with 30-200 mass% of water or chemical solution in an ultrasonic device having a frequency of 20-40 KHZ, power of 100-500 W and a temperature of 20-80 degrees C for 5-45 minutes, adding 20-70 mass% of active sludge and water according to a solid-liquid ratio of 1:5-1:20, adding sodium hydroxide solution to adjust pH value of 6.5-7.5 and then fermenting at 20-55 degrees C for 50 days, and collecting methane drainage gas by gathering method.    USE - The method is useful for processing carbon raw material, which is useful for producing biogas (claimed).    ADVANTAGE - The method rapidly processes the carbon raw material with less energy consumption, and high yield.
NOVELTY - Processing bamboo shoot residue, comprises mechanically crushing the preprocessed bamboo shoot, dissolving obtained powder with sodium hydroxide, washing obtained mixture using water, filtering and collecting solid residue and then drying, performing enzymatic hydrolysis of the solid residue by adding sodium citrate, adding hydrolyzed solid residue to cellulase and hemicellulase at 35-45 degrees C, filtering the residue to obtain sugar reducing liquid, performing detoxification treatment of the reducing liquid by adding active carbon, and fermenting reducing liquid at 30-35 degrees C for 60 hours.    USE - The method is useful for processing bamboo shoot residue for preparing fuel ethanol (claimed).    ADVANTAGE - The method processes the bamboo shoot residue in simple and cost effective manner.    DETAILED DESCRIPTION - Processing bamboo shoot residue, comprises mechanically crushing the preprocessed bamboo shoot using a 20 meshed sieve to obtain powder, dissolving the powder with 1% of sodium hydroxide at 121 degrees C for 30 minutes, washing obtained mixture using water, filtering and collecting solid residue and then drying, performing enzymatic hydrolysis of the solid residue by adding sodium citrate, where the solid-to-liquid ratio is 1:10, adding 8-16% of hydrolyzed solid residue to cellulase and hemicellulase at 35-45 degrees C for 45-60 hours, filtering the residue to obtain sugar reducing liquid, performing detoxification treatment of the sugar reducing liquid by adding 2% of active carbon, and fermenting 50-70 g/l of sugar reducing liquid at a pH of 4.5-6 at 30-35 degrees C for 60 hours.
NOVELTY - Aquiculture fertilizer comprises Bacillus subtilis spores, Bacillus licheniformis spores, Lactobacillus, rapeseed oil residue, oyster powder, carrier, sucrose, slow release compound, sodium natrophenolate and sodium humate, where the carrier includes rice bran, wheat bran and peanut cake, and the mass ratio of the: Bacillus subtilis spores, Bacillus licheniformis spores and Lactobacillus, and rapeseed oil residue is 0.04-0.06:1; rapeseed oil residue and carrier is 0.5-0.8:1; sugar and rapeseed oil residue is 0.06-0.08:1.    USE - Aquiculture fertilizer.    ADVANTAGE - The aquiculture fertilizer can: be rapidly prepared with antibacterial sterilization function; and promote the healthy and sustainable development of aquaculture in green.    DETAILED DESCRIPTION - Aquiculture fertilizer comprises Bacillus subtilis spores, Bacillus licheniformis spores, Lactobacillus, rapeseed oil residue, oyster powder, carrier, sucrose, slow release compound, sodium natrophenolate and sodium humate, where the carrier includes rice bran, wheat bran and peanut cake, and the mass ratio of the: Bacillus subtilis spores, Bacillus licheniformis spores and Lactobacillus, and rapeseed oil residue is 0.04-0.06:1; rapeseed oil residue and carrier is 0.5-0.8:1; sugar and rapeseed oil residue is 0.06-0.08:1; sodium natrophenolate or sodium humate, and rapeseed oil residue is 0.07-0.09:1; slow release compound and rapeseed oil residue is 0.1-0.2:1; and oyster powder and rapeseed oil residue is 0.1-0.2:1.
NOVELTY - Straw carbonization furnace comprises a furnace body (1), where one side of the furnace body is provided with a big furnace door (2) and small furnace door (3). The big furnace door is connected to the furnace body via big furnace door sealing rod (4) and big furnace door hinge (5); and the small furnace door is connected to the big furnace door via small furnace door sealing rod and small furnace door hinge. A cavity is disposed in the furnace body, and the cavity surrounding the furnace body is provided with a water interlayer.    USE - Used as a straw carbonization furnace.    DETAILED DESCRIPTION - Straw carbonization furnace comprises a furnace body (1), where one side of the furnace body is provided with a big furnace door (2) and small furnace door (3). The big furnace door is connected to the furnace body via big furnace door sealing rod (4) and big furnace door hinge (5); and the small furnace door is connected to the big furnace door via small furnace door sealing rod and small furnace door hinge. A cavity is disposed in the furnace body, and the cavity surrounding the furnace body is provided with a water interlayer. The upper end of the water interlayer is connected to the water interlayer outlet port and interlayer water inlet. The upper end of a furnace chamber is provided with a cigarette tube, and the lower end of the furnace body is provided with water interlayer and connected to the hot water outlet pipe and heat pump. The furnace chamber is internally provided with a temperature sensing probe, which is connected with a control device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw carbonization furnace.    Furnace body (1)    Big furnace door (2)    Small furnace door (3)    Big furnace door sealing rod (4)    Big furnace door hinge (5)
NOVELTY - Organic fertilizer comprises raw materials comprising 300-400 kg edible fungi leftovers, 10-50 kg fermenting bacteria fast rotting agent, 50-100 kg bacterial enzymes, 200-250 kg hair hydrolyzate, 5-20 kg urea, 25-50 kg yellow leaves, 5-10 kg brown sugar, 20-100 kg calcium powder, 20-100 kg silicon fertilizer and 50-100 kg attapulgite.    USE - The organic fertilizer is useful for growth of crops.    ADVANTAGE - The organic fertilizer is cost-effective and environmentally-friendly, improves quality of product, saves time and labor, and utilizes waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing the fertilizer, which involves (a) mixing hair and bacteria fast rotting agent, adding 100-200 times water, soaking for 30-100 days, stirring the mixture, further adding 50-100 times water, heating the mixture at 80 degrees C for 1-2 hours, cooling for 30-50 degrees C, heating, cooling, repeating the operation for 2-4 times, adding calcium carbonate powder, and adjusting pH of the mixture to 3-7 to obtain hair hydrolyzate, and (b) adding bacteria fast rotting agent into edible fungus leftovers, further adding hair hydrolyzate, yellow leaves, urea and brown sugar, fermenting the mixture at 50-60 degrees C, raising temperature to 50-80 degrees C, adding enzyme and silicon fertilizer, uniformly mixing the materials, and granulating the mixture to obtain product.
NOVELTY - Preparing in situ organic soil thickening bio-diesel oil, comprises (i) taking 1-10 pts. wt. clay according to 100 pts. wt., 0.8-1.2 times of quaternary ammonium compound according to the cation exchange capacity, and bio-diesel oil (balance), where the quaternary ammonium compound is cationic surfactant, and (ii) mixing clay, quaternary ammonium compounds and bio-diesel oil to prepare the mixed system, lower than the boiling point of organic solvent, heating and stirring the mixed system, dispersing uniformly the quaternary ammonium salt and clay to obtain the thickened bio-diesel.    USE - The method is useful for preparing in situ organic soil thickening bio-diesel oil (claimed).    ADVANTAGE - The method has simple preparation process, consumes less energy, reduces the cost, uses economical bio-diesel oil as base oil, and uses by-product glycerol from biological diesel oil production process and saves the cost.
NOVELTY - Detachable inner and outer hot type biomass pyrolysis furnace comprises a metal furnace shell, metal furnace, ignition oxygenator, stove base, upper and lower horizontal joint double-taper double-sand groove and a vertical splicing fine sand sealer. A flue gas pipe device is set on top plate of the metal furnace shell, and the metal furnace shell is placed inside the metal furnace, and the metal furnace shell is provided with a detachableb pot, and the metal furnace is divided into two halves so as to form an open container.    USE - Used as a detachable inner and outer hot type biomass pyrolysis furnace.    ADVANTAGE - The pyrolyzing furnace is convenient to carry, rapidly discharges drainage, carries out uniform pyrolysis, quickly cools, is simple to operate, and ensures high yield.    DETAILED DESCRIPTION - Detachable inner and outer hot type biomass pyrolysis furnace comprises a metal furnace shell, metal furnace, ignition oxygenator, stove base, upper and lower horizontal joint double-taper double-sand groove and a vertical splicing fine sand sealer. A flue gas pipe device is set on top plate of the metal furnace shell, and the metal furnace shell is placed inside the metal furnace, and the metal furnace shell is provided with a detachableb pot. The metal furnace shell (with more than 2 parts), a metal furnace shell top cover and upper and lower horizontal joint double-taper double-sand groove and the vertical splicing fine sand sealer are provided with a sealing body, and the metal furnace is divided into two halves so as to form an open container.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the detachable inner and outer hot type biomass pyrolysis furnace.
NOVELTY - The furnace has a lower clapboard (24) fixed in a horizontal furnace body (1) that is divided into an upper air chamber (5), an upper combustion chamber (7), a lower combustion chamber (8), a dust depositing chamber (23) and a lower air chamber (6). The upper combustion chamber is provided with axial nozzles (15). A furnace bridge (3) is formed with multiple ash discharging holes (17) and an exhaust hole (18). The lower air chamber is provided with an air inlet (21) and connected with an air pipe (9). A gas outlet pipe (14) is connected with an external gas device fuel inlet.    USE - Double structure biomass gasification furnace.    ADVANTAGE - The furnace improves conversion efficiency of lifting gas and reduces production cost, and has simple structure and improved performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a double structure biomass gasification furnace.    Horizontal furnace body (1)    Furnace bridge (3)    Upper air chamber (5)    Lower air chamber (6)    Upper combustion chamber (7)    Lower combustion chamber (8)    Air pipe (9)    Gas outlet pipe (14)    Axial nozzles (15)    Ash discharging holes (17)    Exhaust hole (18)    Air inlet (21)    Dust depositing chamber (23)    Lower clapboard (24)
NOVELTY - The system has a boiler biomass gasification furnace connected through a gas pipeline that is connected with a boiler. The biomass gasification furnace is provided with a feeding port, and a hop is formed in a reaction chamber and provided with a heating fire grate. A feeding port is connected through a conveying pipeline that is connected with a reaction chamber. The biomass gasification furnace is provided with an ash outlet that is set on bottom of the hop. The feeding port is provided with a sealing cover.    USE - Biomass gasification combustion boiler system for a combustion device.    ADVANTAGE - The system maintains stable steam parameter of the boiler and ensures continuous production process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification combustion boiler system.
NOVELTY - The furnace has a fire blocking ring (2) located in a furnace head (5) that is located in a combustion chamber (7). An upper part of a furnace body (9) is provided with an exhaust port (6). The furnace body is provided with an ash box (12), and a spiral feeding pipe (16) is connected with a motor (17). A spiral feeding pipe is connected with the combustion chamber and provided with a blast pipe (15). The furnace head is provided with an upper hole (4). An air supply passage is provided with a movable wind board (3).    USE - Biomass energy saving furnace.    ADVANTAGE - The furnace has better fuel gasification effect, high fuel utilization ratio and short ignition time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass energy saving furnace.    Fire blocking ring (2)    Movable wind board (3)    Upper hole (4)    Furnace head (5)    Exhaust port (6)    Combustion chamber (7)    Furnace body (9)    Ash box (12)    Blast pipe (15)    Spiral feeding pipe (16)    Motor (17)
NOVELTY - The utility model claims one capable of continuously gasification furnace's ash, feeding port is connected with the upper side face's furnace body, is provided with a first feeding port and a second feeding port on the feeding bracket's upper body's inner cavity is connected with the air outlet pipe is installed on the end wall's furnace body, an ash plate left and right ash plate at the lower end of the inner cavity of the furnace body's through the end wall and the left and right two sides of the furnace body ash plate's inlet is located at the lower end of the furnace body is equipped with air nozzle's number is more than or equal to 1 each row upper air inlet pipe. An ash storage tank is connected with the lower part of the furnace body is opened and the lower end is connected with mortar packing auger in auger is sleeved with a packing auger, the auger is sleeved one the lower end of the ash discharge port. This gasification furnace continuously's ash manufacturing cost is low, the operation is simple, the gasification furnace can work continuously, saves cleaning time, and has popularization value.
NOVELTY - The utility model claims one multifunctional rhizome harvester with high efficiency biomass feeding device. Said efficient multifunctional biomass feeding device comprises a feeding mechanism, a storage bin and the discharging mechanism, a feeding mechanism is set on the feeding port's storage bin, a discharging mechanism is set on the discharging port's storage hopper, wherein the smoke exhaust pipeline is equipped with outer feed mechanism, a storage hopper and a discharging mechanism, and the flue gas pipe's outer are connected to form one flue gas channel, upper close to the smoke pipe interlayer's discharge end of the discharging mechanism is provided with a gasification furnace is connected with the smoke's flue gas inlet, upper close to the smoke pipe interlayer's feeding end of the feeding mechanism is provided with a purifying device is connected's flue gas pipeline, a feeding mechanism sealing mechanism. The utility model realizes the reusing residual heat to avoid residual gas directly discharged's air pollution and ensure the biomass raw material with steady environment is convenient to use and improves the application's efficiency at the same time, prevent the gas flow to ensure the application safety.
NOVELTY - The utility model claims one of gasification furnace slag scraping cutter, a cutter base is fixedly connected on the lower end's's body, the centre of the side of the lower cutter's base is connected with the knife handle, wherein the front cutter body is trapezoid's two sides of knife body is double-blade's shape, is processed with a screw thread on the outer surface's knife handle. The gasification furnace slag scraping knife with the gasification furnace slag-breaking device's peripheral air nozzle can be timely crushing or's large particle slag inlet pipe between the furnace wall, into which the dust or small particle slag discharged in time to ensure the condition's gasification furnace has practical effect.
NOVELTY - This utility model claims one kind of gasification furnace slag breaking device, the locating frame's (5) is fixedly connected to the gasification furnace hearth (1)'s inner side wall of knife rod (3) one's head passes through the locating frame (5)'s centre side of the gasification furnace hearth (1)'s inner cavity, slag breaking knife (2) is installed on the knife handle (3)'s. The gasification furnace hearth (1) the rod's (3) up is processed with screw thread, the gasification furnace (1) is fixedly connected with the outer side wall's (6)'s shaft to the central line of the cutter rod (3)'s central axis, spiral handle (7) is screwed on the cutter rod (3)'s upper screw thread section. This gasification furnace slag breaking device operation is flexible and convenient, it can periodically or aperiodically breaking gasification furnace nozzle's peripheral slag layer, the gasification furnace is stable, prolong the service life of the air nozzle for biomass gasification furnace's various nominal capacity, and has popularization and application value.
NOVELTY - This utility model claims one kind of the combustion furnace by using garbage fuel structure, the garbage fuel comprises wood garbage block set on the inflaming retarding wood garbage block's outer surface, said flame retardant layer is composed of dispersed garbage block on the wooden outer surface of flame retardant particles to form the total volume's flame retardant particle is wood garbage block's total volume 7% to 16%, particles are wood garbage block's exterior surface area 68% to 86% distribution area's wood garbage block outer surface. It effectively solves the problem that the biomass fuel's existing technology is easy to open in the smoldering process, so as to make the conversion efficiency's fuel's combustion-supporting furnace is greatly reduced and the safety accident caused by the problem's fuel smoldering's structure this utility model process is stable, the fuel into the furnace's efficiency is high and the safety is good, it has high's practical value.
NOVELTY - The utility model claims one integrated biomass gasification furnace of stove, comprising a furnace body, a furnace body top sealing, the sealing end is reserved with a feeding port and gas outlet's one round, upper port is provided with a furnace cover, burner located at the top of the furnace body, and the gas outlet of the furnace body inner cavity; the furnace body upper part is provided with a rotary rod, the bottom of the furnace body is set with mortar, mortar with the furnace body cavity through the ash frame, frame middle part is provided with an ash ash discharge port, the lower ash discharge port end is provided with an ash plate, upper plate is provided with an ash slag breaking knife, upper side wall is provided with a mortar with the outside connected's ash door, the gasification furnace upper solution is the whole integrated stove structure, furnace (burner) is directly connected with the gasification furnace body is good for preventing the tar and dust block pipeline, and reduce the production cost by more than 10%.
NOVELTY - The utility model's is applied to biomass fuel gas system's large collective dining hall cooking stove of biomass gasification furnace, a tar filtering and recycling device and cooker is composed of air inlet fuel gas output pipeline with the tar filtering and recycling device's's said biomass gasification furnace, a tar's device for filtering and recycling the cooker is connected between the air outlet and the stove's said tar filtering and recycling device is provided with a fuel gas flow meter, gas flow meter and one for controlling said biomass gasification furnace's control unit. The utility model fully considers the non-environment-friendly's existing equipment, short service life and bad reliability's, by setting device for filtering and recycling tar and recovered to filter the tar in the fuel gas pipeline and the cooker by tar pollution is shortened service life,'s biomass fuel gas tar content of the filter is greatly reduced, which is suitable for centralized gas supply such as long distance transmission, it is very suitable for application to large dining hall cooking stove and so on.
NOVELTY - The apparatus has burner (100) that has an igniter (200), and a reformer (300) surrounding on outer surface of burner. The air pre-heater (400) surrounds the outer surface of reformer, and a hot air outlet unit (500) surrounds outer surface of air pre-heater.    USE - Solid oxide fuel cell (SOFC) processing apparatus for SOFC systems.    ADVANTAGE - Provides simple structure and small size with reduced pollution, saved cost, flexible operation and enhanced performance, since the SOFC apparatus integrates the burner, reformer and heat exchanger all in one, along with cell stacks.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the fuel sprayer.    Burner (100)    Igniter (200)    Reformer (300)    Air pre-heater (400)    Hot air outlet unit (500)
NOVELTY - A solid base catalyst is prepared by using solid waste as silicon source, mixing solid waste with lithium source, granulating to obtain powder, and performing heat treatment.    USE - Preparation of solid base catalyst for manufacturing biodiesel (claimed).    ADVANTAGE - Preparation process reduces burden of waste disposal and cost of buying catalyst and provides help for energy source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biodiesel which involves mixing grease and alcohol, heating to reflux, adding solid base catalyst, performing transesterification, reacting isolated product of transesterification reaction, taking out ester solution, and distilling ester solution to remove residual methanol and water.    DESCRIPTION OF DRAWING(S) - The drawing shows an X-ray diffraction image of a solid base catalyst.
NOVELTY - Recycling Azolla purified biogas slurry comprises accumulating the liquid into solid and liquid excrements of poultry farming formed after separation formation of biogas fermenter and biogas; forming a concentrated slurry and slurry filtrate through the membrane filtration device; filtering liquid flowing through the Azolla biological and Azolla percolating water device; and processing the growth and propagation of the Azolla into feed supply.    USE - Method for recycling Azolla purified biogas slurry (claimed).    ADVANTAGE - The method can achieve large scale farm effluent discharge standards, is non-toxic and harmless, does not produce secondary pollution, and reduces the required slurry consumptive land area by 20-120 times.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for recycling Azolla purified biogas slurry (Drawing includes non-English language text).
NOVELTY - Full supply of fertilizer involves supplying a compound fertilizer having nitrate nitrogen content of 2-4%, ammoniacal nitrogen content of 5-8%, amide nitrogen content of 5-8%, nitrogen controlled-release amount of 6-10%, specified phosphorus/potassium nutrient content, and an organic matter content greater than 6%.    USE - Full supply of fertilizer (claimed).    ADVANTAGE - The method improves efficiency of fertilizer nutrients, ensures full support of crop, increases crop yield and quality, prevents heavy metals, other toxic substances, and hazards caused by Escherichia coli, reduces soil salinity, and improves land fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer, which involves granulating materials containing nitrate, ammonium, amide and urea, supplying ammonia gas, ammoniating, adding phosphorus and potassium, granulating, drying, cooling, and screening.
NOVELTY - A purified valnemulin hydrochloride is prepared by mixing valnemulin-containing ether solution and purified water or distilled water, heating at 40-50 degrees C, stirring for 0.5-1 hour, standing, separating upper liquid, adding ethanol to supernatant solution, stirring for 0.5-1 hour, standing, separating upper liquid, slowly stirring at room temperature for 2-3 hours, precipitating, slowly cooling to 0 degrees C, crystallizing, filtering, and drying.    USE - Method for preparing of purified valnemulin hydrochloride (claimed).    ADVANTAGE - The method is simple, easy, low cost and environment-friendly, and has high product yield. The product has high purity.
NOVELTY - Methanol fuel modifier comprises (in wt.%): dimethoxymethane (56-69), fatty acid methyl ester or fatty acid ethyl ester (8-12), oleic acid (7-10), triethanolamine (5-6), n-butanol (9-12), naphthenic acid (1-2) and corrosion inhibitor (1-2). The obtained fuel modifier is mixed with methanol (15-85%) and gasoline or oil component (15-81%).    USE - Methanol fuel modifier.    ADVANTAGE - The methanol fuel modifier is prepared by simple technique, easy to operate, eco-friendly and cost-effective.
NOVELTY - Biodiesel production involves mixing triglyceride and methanol in the reactor to obtain a mixture. Hydroxyl apatite catalyst (0.02 gram) is added into 40 gram of mixture. The reactor is filled with nitrogen for 15 minutes to remove air. The reaction mixture is heated at 80-300?C for 2-12 hours. The obtained mixture is stirred with speed of 600 rotations per minute. The obtained mixture is filtered and extracted to obtain biodiesel. The content of the biodiesel is obtained by using gas chromatography.    USE - Catalytic method for producing biodiesel (claimed).    ADVANTAGE - The catalytic method enables to produce biodiesel with high activity and stability in a simple manner.
NOVELTY - Comprehensive utilization of agricultural and forestry waste resources comprises preprocessing collected agricultural and forestry waste, conveying to separating device, steam cooking, carrying out multi-stage washing, solid-liquid separating, separating hemicellulose, using hemicellulose-enriched liquid for anaerobic fermentation to generate marsh gas or furfural product, and subjecting separated solids to secondary separation.    USE - Comprehensive utilization of agricultural and forestry waste resources used for preparing biomass fuel products and solid biochemical lignin products (claimed).    ADVANTAGE - The method is low cost, environment-friendly and highly efficient.    DETAILED DESCRIPTION - Comprehensive utilization of agricultural and forestry waste resources comprises preprocessing collected agricultural and forestry waste, conveying to separating device, steam cooking at 0.6-3.0 MPa for 1-5 minute, carrying out multi-stage washing, solid-liquid separating, separating hemicellulose from waste resources, using hemicellulose-enriched liquid for anaerobic fermentation to generate marsh gas or furfural product, and subjecting separated solids to secondary separation. The hemicellulose-enriched liquid is processed by precipitating, acidifying, adjusting system, entering into anaerobic fermentation to generate marsh gas, and entering biogas slurry into aerobic and advanced treatment system.
NOVELTY - Composite microbial fertilizer comprises 7-9 wt.% active functional bacteria, 1-3 wt.% soil conditioner, 40-50 wt.% organic fertilizer, and 40-50 wt.% inorganic fertilizer component, where sum of the composite microbial fertilizer 100 wt.%.    USE - The composite microbial fertilizer is useful for sugarcane (claimed) for promoting growth and enhancing stress resistance.    ADVANTAGE - The composite microbial fertilizer increases soil nutrient content, reduces fertilizer using amount, improves utilization ratio of fertilizer to 32%, and improves sugar cane production by 25%, and sugar degree to 1-2 degrees Brix.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composite microbial fertilizer.
NOVELTY - The hydrogen generator has a sealing ring embedded in a fixing ring, and a first cooling unit (110) set on a control device. A second cooling unit (120) is set in the electrolytic groove. The first cooling unit and second cooling unit are connected with a second liquid passage (102). The electrolytic cell (100) and second cooling unit are connected between third fluid passage (103) and first gas channel (121). The second cooling unit and safety protection device (150) are connected with a second air channel (122).    USE - Hydrogen generator for producing hydrogen.    ADVANTAGE - Allows saving maintenance and replacement costs of the hydrogen generator and ensures more stable and reliable operation since service life of the high temperature resistant sealing ring is prolonged. Enhances cooling effect of the electrolytic cell by increasing the effect of gas-liquid separation due to use of multi-cooling system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen generator.    Electrolytic cell (100)    Second liquid passage (102)    Third fluid passage (103)    First cooling unit (110)    Second cooling unit (120)    First gas channel (121)    Second air channel (122)    Safety protection device (150)
NOVELTY - Charcoal preparation involves heating the plant biomass contained in a carbonization reactor with gas outlet at 400 degrees C, and increasing the temperature of the carbonization reactor to 600 degrees C. The heated plant biomass is carbonized in absence of oxygen. The temperature of the carbonization reactor is lowered, and charcoal is obtained from the carbonization reactor.    USE - Method for preparing charcoal from plant biomass.    ADVANTAGE - The method enables preparing charcoal with good quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for preparing charcoal from plant biomass.
NOVELTY - Method of determining the ratio of the total amount of free moisture contained in peat mass to moisture released therefrom by sedimentation involves collecting a representative sample from the extracted peat mass, mixing the sample and collecting multiple samples from different segments of the common sample, repeated mixing, centrifuging and then drying the obtained residue. Before centrifuging, the sample is divided into two parts, one of which is the control part and the other is placed in glass cylinders for one day, after which the amount of freely released moisture is determined. The remaining residue is centrifuged and dried, followed by calculation of the ratio of moisture released by sedimentation to the total amount of free moisture.    USE - Chemistry.    ADVANTAGE - Invention increases the accuracy of determining properties of the peat mass overall.
NOVELTY - The device has a modular area for processing peat supplied to a separator and a crusher. Peat processing lines are installed parallely. Shop storage of raw material, and a frozen peat preparation area installed downstream the crusher are provided in a preparatory. The processing lines are provided with serially interconnected conveyer of roller-toothed crusher having a drum dryer. A storage dispenser of peat and a storage dispenser of lime are connected with mixer. A press-extruder is serially connected with a peat plates forming area, a tunnel dryer, and an engraftment area.    USE - Device for processing peat.
NOVELTY - Joint cracking vacuum gas oil and vegetable oils comprises processing 1-10 wt.% of vacuum gas oil under catalytic cracking condition at 430-470 degrees C using microspherical catalyst containing ultrastable Y zeolite as an active component and a mixture of bentonite clay, amorphous silica and aluminum hydroxide as a matrix, where a ratio of catalyst to feed is 4.    USE - The method is useful for joint cracking vacuum gas oil and vegetable oils (claimed).
NOVELTY - The invention relates to a hydrogen generator which uses water and a solid electrolyte. According to the invention, the generator comprises an electrolyzer (A) provided with a non-metal support (1) wherein there are fixed a metal body (2) and an electrode-pipe (3) with a water intake nozzle ( c) connected to an electrically operated valve (8) controlled by a level detector (9) and an electrolytic assembly with porous electrodes of sintered metal powder with a catalytic layer, preferably Ni or Ni-Fe, and a medial solid electrolyte (4) arranged as an electrolytic sandwich in the shape of a rosette or a spiral, provided with some spacers (I) as small plates which are heat resistant on one face. Above the electrolytic sandwich there is fixed a selective hydrophobic membrane (6), the created Brown's gas being discharged through a tube (d) of a non-metal cap (5). The electrolyzer (A) also comprises a solenoid winding (7) of a transformer with a primary (e) and a secondary winding (e'), with a rectifying diode and the ends connected to the electrode-pipe (3) and to the body (2), placed either on the metal body (2) or at the bottom of the electrode-pipe (3), which is partially filled with thermally conductive powder (j) for storing thermal energy produced by the induction micro currents generated by the electromagnetic field generated inside the electrolyzer (A) and for producing hot water or steam which passes into the electrolysis space through some orifices ( r) in the electrode-pipe (3). In particular, for steam producing purposes, the electrode-pipe (3) or the metal body (2) has the shape of a microwave guide for a microwave generator (B) of the type of resonant cavity (10) with a magnetron (11), the generated microwaves heating some thermally conductive granules (j') made of porous ceramic or carborundum.
NOVELTY - The power-engineering complex structure has a programmer that is designed to control operation mode of a gas-piston power unit. An air flow rate regulator is connected with the power unit and provided to control coefficient of flow rate of air in predetermined range. A remainder mixer is connected with the power unit and a heat exchanger. A granulated biofuel torrefier reactor is provided to heat-transfer the gases obtained from the remainder mixer.    USE - Power-engineering complex structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the power-engineering complex structure.
NOVELTY - Solid acid catalyst obtained by adding acid into bio-charcoal derived from defatted algae, is new, where the bio-charcoal is obtained by plasticizing the microalgae.    USE - The solid acid catalyst is useful for producing biodiesel (claimed) that is used for a diesel engine.    ADVANTAGE - The solid acid catalyst has high stability, is capable of producing biodiesel in a cost-effective manner, and can be reused efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing solid acid catalyst.
NOVELTY - Preparation of Miscanthus pellet, involves (a) pre-treating Miscanthus, and crushing to obtain powder, (b) compressing the powder by adding 220-250 g/l water, and (c) squeezing mixture, and formulating the mixture to pellet form.    USE - The method is useful for preparation of Miscanthus pellet with high calorific value, density and moisture content (claimed).
NOVELTY - Forming a distillate fuel product involves: subjecting a feedstock to a Group VIII metal on molecular sieve catalyst, where the feedstock is selected from biodiesels, lipids derived from vegetable oils, algae oils, and animal fats, and mixtures; and catalytically reacting the feedstock over the catalyst at a temperature of 650-775 degrees F to produce the distillate fuel product.    USE - The method is useful for forming a distillate fuel product (claimed).    ADVANTAGE - The method is a single step process eliminating the need of a separate costly hydrotreating step while producing a renewable source distillate fuel.    DETAILED DESCRIPTION - Forming a distillate fuel product involves: subjecting a feedstock to a Group VIII metal on molecular sieve catalyst, where the feedstock is selected from biodiesels, lipids derived from vegetable oils, algae oils, and animal fats, and mixtures; and catalytically reacting the feedstock over the catalyst at a temperature of 650-775 degrees F to produce the distillate fuel product, where the step of catalytically reacting the feedstock comprises catalytically cracking off its C3 backbone linkage to create individual chains, removing molecular oxygen from the feedstock, saturating double bonds in the chains, and isomerizing the product over the catalyst.
NOVELTY - The apparatus (100) has a laser beam irradiation unit that irradiates a laser beam to gas in a to-be-measured region (20). Mirrors (M1-Mn) are configured to reflect the laser beam irradiated by laser beam irradiation unit. Retro-reflector (RR1) is provided to reflect reflected laser beam. Light quantity measurement unit (40) is provided to measure light quantity of laser beam which it reflected by several mirror and retro-reflector. Calculating unit (50) is set to calculate the concentration of predetermined gas in to-be-measured region based on the measured light quantity.    USE - Gas-concentration-measurement apparatus for methane gas or carbon dioxide gas (all claimed).    ADVANTAGE - The concentration of the measurement of gas can be determined easily, even if the some of the mirror vibrates and the installation angle changes. The difference of the wind measurement position and methane concentration measurement position can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual view of the gas-concentration-measurement apparatus. (Drawing includes non-English language text)    To-be-measured region (20)    Light quantity measurement unit (40)    Calculating unit (50)    Gas-concentration-measurement apparatus (100)    Mirrors (M1-Mn)    Retro-reflector (RR1)
NOVELTY - Additive comprises 50 mass% of partial esters of polyols comprising 1-10 ester units, 1-10 hydroxylated units and 0-6 ether units, where the additive has a sulfur content of less than or equal to 500 parts per million (ppm) by weight.    USE - The additive is useful for limiting the deposition of soap and/or varnish in internal parts of direct injection engine systems for biodiesel type fuel (claimed).    ADVANTAGE - The additive can avoids and prevents the formation of soap and/or varnish deposits in the internal parts of injection engine systems thus maintaining the cleanliness of the engine and improving the wear resistance and lacquering resistance of superior quality diesel or biodiesel fuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) use of the additive for limiting the deposition of soap and/or varnish in internal parts of injection engine systems for biodiesel type fuel;    (2) a biodiesel type fuel composition comprising the additive and optionally at least other functional additives such as deposition reducers, detergents and/or dispersants, anti-oxidants, combustion improvers, corrosion inhibitors, additives resistant to cold, dyes, demulsifiers, metal deactivators, antifoaming agents, agents for improving cetane number, lubricity additives, antiwear agents, friction modifiers, co-solvents and compatibilizing agents; and    (3) limiting the deposition of soap and/or varnish in internal parts of injection engine systems for biodiesel type fuel comprising combusting a composition in the engine.
NOVELTY - A system (10) has a collection subsystem (12) to collect a gaseous mixture comprising carbon dioxide and methane, a combustion subsystem (14) to combust methane in the gaseous mixture and to eject a gaseous combustion effluent, and a separation subsystem (16) to separate the carbon dioxide from the gaseous combustion effluent. The combustion subsystem generates electrical energy, water and additional quantities of the carbon dioxide.    USE - System is used for processing greenhouse gases (claimed) e.g. methane, carbon dioxide, water vapor, and ozone, and for producing electrical energy, carbon dioxide, and water.    ADVANTAGE - The system effectively eliminates the release of greenhouse gases from landfills.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing greenhouse gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of flowchart for processing greenhouse gases.    System (10)    Collection subsystem (12)    Combustion subsystem (14)    Separation subsystem (16)    Process gas (20)
NOVELTY - A Nostoc sp. strain KNUA003 (KCTC 12063BP) capable of producing heptadecane, hexenol and 16-18C fatty acid, is new.    USE - The Nostoc sp. strain is useful for producing heptadecane, hexenol and 16-18C fatty acid (claimed), and biodiesel.
NOVELTY - Hydrogen generator unit comprises a replacement cartridge unit for generating low-pressure hydrogen from water, where the generator unit includes two reaction chambers which are adapted to employ an extracting chemical process to generate low-pressure hydrogen from water in an exothermic reaction in a cartridge-based system, where the cartridge-based system has a membrane separating the two reaction chambers, and where the cartridge unit has a start-and-stop functionality.    USE - The hydrogen generator unit is useful in on-vehicle system (claimed), preferably for standalone energy systems or for use in on-vehicle systems in conjunction with either fuel cell or internal combustion engine.    ADVANTAGE - The hydrogen generator unit can improve storage and generation of hydrogen gas on demand.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of generating hydrogen using a hydrogen generator unit including a compression unit for generating low-pressure hydrogen from water, involving providing a replacement cartridge unit including one or more composite materials, and which is connected to a water storing unit, the replacement cartridge unit being operable to generate hydrogen; where the method further includes supporting, using the replacement cartridge's lower housing, an exothermic reaction involving the one or more composite materials and water supplied from the water storing unit to generate the Hydrogen, where one or more composite elements are enclosed in the replacement cartridge's lower housing unit which is adapted to be disposed of or recycled after use in the hydrogen generator unit; or a method of generating hydrogen from a hydrogen generator unit, involving employing a replacement cartridge unit which includes two separate chambers which can be connected to a water storing unit, and also temporary store and arrangement to compress generated hydrogen.
NOVELTY - Preparing tegaserod maleate, comprises: (a) carrying out alkylation reaction of aminothiourea with an alkylating reagent in ethanol in the presence of a catalyst to obtain S-methyl-amino-isothiourea, (b) reacting S-methyl-amino-isothiourea and n-pentyl amine in ethanol to synthesize N-pentyl-N-aminoguanidine, (c) carrying out condensation reaction of N-pentyl-Naminoguanidine and 5-methoxy-indol-3-aldehyde under acidic condition to obtain tegaserod, and (d) salifying tegaserod and maleic acid in a mixed liquid of ethanol and ethyl acetate to obtain a crystal i.e. tegaserod maleate.    USE - The method is useful for preparing tegaserod maleate (claimed).    ADVANTAGE - The method is economical, does not adopt rigorous reaction condition or use highly toxic reagents, and ensures improved yield, and thus suitable for industrial production.
NOVELTY - Method for producing microorganic fertilizer, involves preparing deodorizing microorganic composition, useful microorganic composition and microorganic base compost, and blending mixture with nitrogen, phosphorus, and potassium (NPK) fertilizer to obtain microorganic fertilizer.    USE - The method is useful for producing microorganic fertilizer.    ADVANTAGE - The method employs microorganic composition for deodorizing organic materials for enhancing temperature, reducing unpleasant odor, shortening fermenting time, and improving quality of the compost pile, thus increasing labor productivity. The organic materials are simultaneously treated with organic separating yeast, added with phosphate separating microorganisms, nitrate fixing microorganisms, humic acid and microelement mixture and with NPK proportions suitably balanced for each type of plants and specific area of land for creating a high quality microorganic fertilizer to serve in safe and sustainable agricultural development.
NOVELTY - Method for preparing oil from microorganisms involves (a) culturing the microorganisms in a culture medium, (b) concentrating the culture medium containing culture by spin-drying, (c) subjecting the concentrate to cytoclasis in which cells of the microorganism are destroyed, where the cytoclasis is performed by freezing the obtained cells for predetermined time, refrigerating the frozen mixture at predetermined temperature, concentrating the frozen culture and overcooling the concentrate, and (d) separating and recovering oil from the destroyed microbial culture.    USE - The method is useful for preparing oil from microorganisms which is useful for producing hydrocarbon (claimed).    ADVANTAGE - The method consumes minimal energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for preparing oil from the microorganisms, which comprises culturing unit for culturing the microorganisms in a culture medium, concentrating unit for performing spin-drying and concentrating, cytoclasis unit for destroying cell of microorganisms, and oil separation-and-recovery unit for recovering oil.
NOVELTY - Cellulose biomass feedstock is saccharified by solubilization process by converting biomass feedstock which contains cellulose into solubilized mixture by controlling temperature, pressure, and water content ratio and controlling the generation amount of organic acid, controlling pH by adjusting water quantity, and saccharification process by hydrolyzing solubilized mixture to obtain saccharified liquid.    USE - A saccharification method of cellulose biomass feedstock (claimed).    ADVANTAGE - Acidic catalyst is not required, process steps is reduced, and manufacturing cost is cheap.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for saccharification apparatus for performing saccharification of cellulose biomass feedstock comprising saccharification unit which heat-processes the aqueous solution obtained after the solid-liquid separation to obtain saccharified liquid, 1st and 2nd obstruction removal unit filled with cation exchange substance, 1st flow path where aqueous solution flows into the 2nd obstruction removal unit via the saccharification unit from the 1st obstruction removal unit, 2nd flow path where aqueous solution flows into the 1st obstruction removal unit via the saccharification unit from the 2nd obstruction removal unit, and switch unit which enables switching of the 1st flow path and the 2nd flow path.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the saccharification method of biomass feedstock. (Drawing includes non-English language text).    Coarse grinding process (S1)    Water content adjustment process (S2)    Solubilization process (S3)    Extraction process (S4)    Saccharification process (S5)
NOVELTY - B-alkyl substituted ammonia borane compound is new.    USE - For releasing hydrogen from the compound (I) (claimed) for replacing petroleum as the primary fuel for transportation and remote power applications; as hydrogen storage materials which is used in or with a hydrogen-powered vehicle, such as an automobile.    ADVANTAGE - The compound (I) detailing hydrogen release conditions, and characterization and regeneration of spent-fuel material.    DETAILED DESCRIPTION - B-alkyl substituted ammonia borane compound of formula (I) is new.    R1=H or optionally substituted alkyl;    R2=optionally-substituted alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) a hydrogen storage system comprising the compound (I); and    (2) releasing (M1) hydrogen from the compound (I) involving: heating the compound (I), contacting the compound (I) with a catalyst, or simultaneously heating the compound (I) and contacting the compound (I) with a catalyst.
NOVELTY - The method involves reacting animal fats or vegetable oils used either pure or with an alcohol at 0-300 degrees C for 10 minutes to 24 hours in presence of a solid catalyst. The animal fats or vegetable oils are treated with calcium hydroxide, calcium oxide, calcium alkoxide, calcium diglyceroxide or their mixture for forming alkyl esters fatty acid, which is separated from unreacted alcohol and glycerin by decantation, filtration, centrifugation or solid-liquid extraction.    USE - Method for performing transesterification reactions in heterogeneous phase for obtaining fatty acid alkyl esters or glycerol, preferably biodiesel.
NOVELTY - Preparation of high-germination rate biomass carbon breeding material comprises collecting organic materials, drying, crushing, sealing in jar to carry out hypoxia, carbonizing to 250-650 degrees C for 3-6 hours, and sieving.    USE - Method for preparation of high-germination rate biomass carbon breeding material used as paddy rice or corn seedling breeding material (claimed).    ADVANTAGE - The method turns waste into treasure, reduces environmental pollution, provides good material for agricultural nursery, and has good economic effects.