NOVELTY - Household food residue processing apparatus comprises residue cleaning device, filtering device, drying device and grinding device, where residue cleaning device comprises cover (1), shaft (2, 3), spring (4) and an electromagnet (5). The filter device comprises hole pipe (6), oil cotton (7), filter screen (8), water inlet end (9), water outlet end (10), water flow measuring hole (11) and stop valve (12). The drying device comprises external residue entrance (13), heating silk (14), fan (15), flange (16), temperature sensor (17) and butterfly valve (18).    USE - Household food residue processing apparatus used for reducing liquid and solid garbage.    ADVANTAGE - The household food residue processing apparatus reduces environmental pollution by reducing domestic garbage, ensures rapid processing and preparation of residue dry fertilizer powder for planting bonsai.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of household food residue processing apparatus.    Cover (1)    Shaft (2, 3)    Spring (4)    Electromagnet (5)    Hole pipe (6)    Oil cotton (7)    Filter screen (8)    Water inlet end (9)    Water outlet end (10)    Water flow measuring hole (11)    Stop valve (12)    External residue entrance (13)    Heating silk (14)    Fan (15)    Flange (16)    Temperature sensor (17)    Butterfly valve (18)
NOVELTY - Processing municipal sludge involves concentrating active municipal sludge to control water content, where sludge is fermented with energy grass anaerobically to generate marsh gas for power generation or biological natural gas. The fermented material is separated into solid-liquid to obtain biogas residue and biogas. The biogas sewage is returned into continued recycling process for producing marsh gas for generation of power. The water content of sludge is controlled to obtain processed mud.    USE - Method for processing municipal sludge used as soil improving agent (claimed).    ADVANTAGE - The method enables to process municipal sludge that ensures increased value of sludge.
NOVELTY - Organic fertilizer comprises 30-50 pts. wt. peat, 30-50 pts. wt. rice hull, 10-20 pts. wt. starch, 10-20 pts. wt. soybean powder, 10 to 20 pts. wt. plant protein, 10-20 pts. wt. humic acid, 10-30 pts. wt. potassium carbonate, 1-10 pts. wt. polyacrylamide, 10-20 pts. wt. calcium superphosphate, 3-10 pts. wt. urea, 10-20 pts. wt. diatomite, 1-5 pts. wt. nano carbon powder, 10-20 pts. wt. cellulose and 10-20 pts. wt. composite microbial inoculum.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer increases soil water retaining property, quick absorption, crop yield and fertilizer effect, and ensures low investment, low energy consumption and no pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) crushing peat, rice hull and diatomite in pulverizer to obtain mixture;    (B) fermenting composite microbial inoculum, starch and soybean powder mixture in tank for 30 hours below 38 degrees C to obtain composite liquid;    (C) mixing composite liquid with obtained mixture, plant protein, humic acid, potassium carbonate, polyacrylamide, calcium superphosphate, urea, nano carbon powder and cellulose in a mill at 200-300 revolutions per minutes for 30 minutes; and    (D) granulation obtained mixture using granulator to obtain product.
NOVELTY - Preparing potted soil involves crushing water-absorbing material to obtain particles that is mixed with peat in volume ratio of 1:1-1:5 to obtain product.    USE - Method for preparing potted soil (claimed).    ADVANTAGE - The method enables to prepare potted soil in simple, and cost-effective manner, and ensures stable performance, enhanced soil water-retaining effect, increased quality of potted flower and reduced environmental pollution.
NOVELTY - Organic fertilizer comprises 40 wt.% willow branch, 10 wt.% rapeseed flower honey, 40 wt.% rice vinegar, 10 wt.% spiral algae extract, 1 wt.% copper ammonium complex and 0.1-0.2 wt.% fermentation agent i.e. Aspergillus niger or brewer's yeast.    USE - Organic fertilizer used for planting tomato (claimed).    ADVANTAGE - The organic fertilizer promotes root development, and ensures lush foliage, fruit color and easy absorption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) boiling willow branch with water at small fire at 30 degrees C;    (B) filtering boiled materials to obtain extract;    (C) fermenting obtained extract at 28-32 degrees C for 3-4 days;    (D) mixing rapeseed flower honey and rice vinegar with fermented material at 35-40 degrees C for 24 hours; and    (E) stirring obtained materials with spiral alga extract and copper ammonium complex for 0.5 hours at 108 revolutions/minute to obtain product.
NOVELTY - Preparing organic soil for seedling vegetable involves crushing 2-3 parts vinegar residue, 2-3 parts cassava residue, 1-2 parts mixed organic material, 3-5 parts aged soil mixture, 1-2 parts coconut, 1-2 parts river or pond mud or frozen earth, 1-2 parts bran, 0.5-1 parts vermiculite and 0.5-1 parts perlite to obtain powder. Agaricus bisporus is mixed with 0.1-0.3% ternary compound fertilizer and powder to carry out anaerobic fermentation process at 68-70 degrees C for 2 days in a fermentation groove with length of 50-150m, width of 5-6m, height of 1.3-1.6m and thickness of 10-20cm.    USE - Method for preparing organic soil for seedling vegetable (claimed).    ADVANTAGE - The method enables to prepare nutritious organic soil, which is brown or black brown granules without peculiar smell.    DETAILED DESCRIPTION - Preparing organic soil for seedling vegetable involves crushing 2-3 parts vinegar residue, 2-3 parts cassava residue, 1-2 parts mixed organic material, 3-5 parts aged soil mixture, 1-2 parts coconut, 1-2 parts river or pond mud or frozen earth, 1-2 parts bran, 0.5-1 parts vermiculite and 0.5-1 parts perlite to obtain powder. Agaricus bisporus is mixed with 0.1-0.3% ternary compound fertilizer and powder to carry out anaerobic fermentation process at 68-70 degrees C for 2 days in a fermentation groove with length of 50-150m, width of 5-6m, height of 1.3-1.6m and thickness of 10-20cm. Mixed organic material comprises nitrogen, phosphorus and potassium elements. Microbial inoculum is added in the fermentation process, where microbial inoculum (0.5-1 hundred million/g) comprises actinomycetes, yeast, lactic acid.
NOVELTY - Preparing organic matrix involves drying and crushing 3-6 parts manioc waste and straw powder, 1-2 parts coconut bran, 1-2 parts plant ash, 1-2 parts grass carbon and 0.5-1 parts vermiculite to obtain a mixture. 25-35 wt.% Vinegar residue, 40-50 cassava residue and 15-25 straw are added in the mixture and then microbial inoculum containing beneficial microorganism is added to carry out fermentation at 68-70 degrees C for 3-5 days. The fermentation product is dried and crushed, and then packaged and sealed.    USE - Method for preparing organic matrix used for planting rice seedling (claimed).    ADVANTAGE - The method enables to prepare organic matrix that promotes rice seedlings growth.
NOVELTY - Preparing organic matrix granules involve drying and crushing 70-90% corn core, 5-15% vermiculite and 5-15% plant ash or carbonized rice bran into powder with particle diameter of 6mm. Beneficial microorganism fermentation microbial inoculum is mixed with powder, and then fermentation is carried out for 30-60 days in a fermentation groove having depth of 1-1.2m. The fermentation product is dried, crushed, and then packaged and sealed.    USE - Method for preparing organic matrix granules used for planting potted flower (claimed) and ornamental plant.    ADVANTAGE - The method enables to prepare organic matrix that replaces porcelain granules, grass peat and nutrients of earth, and has improved air permeability.
NOVELTY - Matrix composition is prepared by crushing and mixing pepper straw, corn rice straw and cow dung in ratio of (0-3):(4-7):(1.5-4.5) to obtain a mixture. The mixture is mixed with water in ratio of 1:1.5-4, and then fermentation is carried out at 50-60 degrees C in a fermentation pool having width of 3m and height of 1.8-2m. The fermentation pool temperature is 65 degrees C, where pH value of the fermented product is 6.0-7.6.    USE - Matrix composition used for soilless cultivation of seedling (claimed).    ADVANTAGE - The matrix composition is cost-effective and eco-friendly, reduces overexploitation of non-renewable resources, and replaces grass carbon.
NOVELTY - Fixation agent comprises 30-50 wt.% bamboo charcoal powder, 3-5 wt.% ferrous sulfate, 10-15 wt.% calcium superphosphate and filling agent. Filling agent is brown algae.    USE - Fixation agent used for controlling loss of nicotine in tobacco during compost process (claimed).    ADVANTAGE - The fixation agent reduces nitrogen loss and problem of odor while composting.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling loss of nicotine in tobacco during compost process, which involves:    (A) mixing tobacco waste and livestock manure as compost materials and stirring uniformly;    (B) mixing 4-5% fixation agent with compost materials; and    (C) adding water with the mixture and composting through fermentation.
NOVELTY - Preparing solid organic fertilizer involves removing impurities from fresh chicken manure. The obtained chicken manure and water are mixed to obtain mixture that is dehydrated using machine to control water content of 44-52%. The dehydrated manure is fermented at 25-30 degrees C for 2-5 hours and then at normal temperature for 20-25 days to obtain semi-finished product that is dried (water content 10-12%) and pelletized to obtain solid organic fertilizer.    USE - Method for preparing solid organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare solid organic fertilizer that improves soil physical and chemical property, promotes plant growth and soil ecological balance, and reduces chicken waste discharge problem in cost-effective manner.
NOVELTY - Homemade detergent comprises 2 pts. wt. sugar, 2-3 pts. wt. fresh plant kitchen garbage, 7-10 pts. wt. water and 1-2 pts. wt. pandan leaves.    USE - Homemade detergent.    ADVANTAGE - The homemade detergent is environment-friendly, and has fragrance smell and strong clean ability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing homemade detergent, which involves adding sugar, fresh plant kitchen garbage, water, egg shell, orange peel, lemon peel and pepper in a fermentation container, sealing the container for 2 months for fermentation at room temperature, and filtering the fermented liquid to obtain the desired product; and    (2) a fermentation container, which comprises round container main body, providing bottom of the container main body with filter network, and providing the container main body with an exhaust valve.
NOVELTY - This utility new type relates to one used for a mechanism of improved carbon kiln, comprising kiln body, internal of the kiln body provided with containing space, and the top part of kiln body provided with penetrate water of kiln, the kiln provided with lighting window and the containing space and connected, the kiln is further provided with sand groove and cover sand layer has. A water spray pipe through the permeability layer entering into a kiln internal, cooling the kiln internal temperature, and take away evaporation of water vapour through the ignition window, using kiln comprises a kiln top and to the permeability of a cooling operation, accelerates the kiln internal and external heat exchange of a velocity so as to effect a rapid cooling, and cooling after o carbon good product, finished product rate is high, operation stable and reliable safety.
NOVELTY - This utility new type claims a a biomass pyrolysis and gasification of garbage fuel reactor, comprising: the first rotating shaft, the second rotating shaft, multiple , the second rotating shaft and the first rotating shaft are connected, and the first rotating shaft and a rotating the same, a located on a second rotating shaft, and the and the second rotating shaft fixing connection, the and the second rotating shaft are both adopt stainless steel material. By a method, this utility new type is a biomass pyrolysis and gasification of garbage fuel reactor A, can better use of biomass fuel raw material and reactor design has simple structure, easy operation, it can further reduce a cost and improves reaction efficiency.
NOVELTY - This utility new type claims a a lower sucking type biomass gasification furnace, burning biomass raw material for a gas fuel, comprising a, a furnace body, a side upper wall has equipped with multiple used for introducing combustion-supporting air of air inlet hole, lower furnace body, set at the lower part of a furnace body, a device, set in the lower furnace body up, used for input the biomass raw material after a reaction of gas fuel air supply device, and the air inlet hole connected, is used for the biomass raw material of combustion supply steam combustion-supporting a set ratio of a combustion-supporting gas combustion-supporting air of the inner, the steam through a lower combustion-supporting furnace waste heat as a heat source of a, the utility model is new in type of gasification furnace, by side-introducing combustion-supporting gas, solves the problem that the biomass material combustion uniformity problem is. By using combustion-supporting gas of a steam, reducing the nitrogen content in a gas fuel. The furnace body using a waste heat steam combustion-supporting, saves the energy, saves the device cost.
NOVELTY - This utility new type claims a a lower sucking type biomass gasification furnace, burning biomass raw material for a gas fuel, comprising a, a furnace body, a side upper wall has equipped with multiple used for introducing combustion-supporting air of air inlet hole, lower furnace body, set at the lower part of a furnace body air supply device, the air inlet hole and connected, used for a raw material of biomass combustion supply steam combustion-supporting a set ratio of a combustion-supporting gas combustion-supporting air of the inner, the steam combustion-supporting gas fuel carry through waste heat as a heat source of a device, a device, set in the lower furnace body up, used for input the biomass raw material after a reaction of gas fuel. This utility new type in a lower suction type biomass gasification furnace, by side-introducing combustion-supporting gas, solves the problem that the biomass material combustion uniformity problem is. A combustion-supporting gas by a steam, reducing the nitrogen content in a gas fuel. Using gas fuel a combustion waste heat steam, saves the energy, saves the device cost.
NOVELTY - This utility new type claims a biomass drying environment-friendly integrated one rod device, composed of a two set in parallel set with a forming machine device, two forming machine device set a. air processing device has a fume air blower, the forming machine is comprise in sequence a b c a, with, sieving device, a feeding packing auger, a burner, a three layer dryer, buffer, feeding blower, separator, separator by a material tube connection has two parallel set with a table machine, welding table two rod machine by branch pipe has a flue pipe, smoke and fume air blower connecting pipe, upper end and upper end of buffer of the separator has a dust suction air blower, a dust air blower and air treatment device connection. This utility new type production is large, can adapt to large scale production is needed, further can a large amount of dust and fume production process in a product and then emptying after collective processing, to reduce atomphere pollute.
NOVELTY - The invention claims an ecological cultivating cowhouse, comprising a semi clock building shape roof, a cowshed body. Cultivating project of a whole cowhouse, a house in natural air, air fresh. The novel fermentation pool floor design, reduces the cattle excrement to environment is pollute, obvious increase disease resistance ability of cow, reduce the investment of lying fence, the dung excrement processing system and a device of cattle, the excrement cleaning and processing link of cattle, it saves a charge, and reducing cultivation cost to reach the purpose of cleaning at the same time filler and can as organic fertilizer use, protecting the environment and increase the economic benefit.
NOVELTY - A planting green fertilizer comprises 40-60 pts. wt. straw, 10-20 pts. wt. animal waste, 5-15 pts. wt. calcium superphosphate, 5-10 pts. wt. potassium sulfate, 1-5 pts. wt. chitosan, 2-6 pts. wt. sodium alginate, 5-15 pts. wt. soybean meal, 2-4 pts. wt. bioenzyme and 2-4 pts. wt. organic fertilizer leavening agent.    USE - Planting green fertilizer (claimed).    ADVANTAGE - The safe and clean planting green fertilizer improves crop quality and yield, protects soil, and reduces use of chemical fertilizer and pesticide, provides amino acids, ribonucleic acid, calcium, trace minerals and other nutrients required for growing crops. The fertilizer improves long-standing reliance on chemical fertilizer and pesticide in agriculture. The fertilizer provides excellent disease resistance to crops.
NOVELTY - Fertilizer comprises composition (A) and composition (B). The composition (A) comprises 0.01-0.05 pt. wt. carbendazim, 0.005-0.01 pt. wt. monocrotophos, 35-40 pts. wt. urea, 25-30 pts. wt. calcium biphosphate, 18-25 pts. wt. potassium sulfate, 3-8 pts. wt. zinc sulfate, 0.5-2 pts. wt. borax and 0.5-1 pt. wt. ammonium molybdate. The composition (B) comprises 10-15 pts. wt. sesame leaves, 5-10 pts. wt. peanut, 15-22 pts. wt. alfalfa, 8-15 pts. wt. plant ash, 30-35 pts. wt. turves, 15-22 pts. wt. human and animal excreta, and 1-3 pts. wt. effective microorganism (EM).    USE - The fertilizer is useful for cultivation of sesame (claimed).    ADVANTAGE - The fertilizer has improved durability, reduces usage of inorganic fertilizer, and cost-effectively improves yield of sesame, and soil fertility.
NOVELTY - Method for treating landfill leachate involves mixing straw powder and landfill leachate, subjecting the mixture to anaerobic fermentation, to obtain wetland biogas residue, dehydrating wetland biogas residue, drying and incinerating.    USE - Method for treating landfill leachate (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables efficient treatment of landfill leachate with reduced leachate stock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for landfill leachate treatment system.
NOVELTY - Household kitchen garbage processor comprises bucket groove (10) in crushing unit, vacuum device (20), deodorization pool (30), seal cover (40) and power device (50). Bucket groove is set in seal inner housing and seal cover. The vacuum device comprises a vacuum pump and pipe that is provided with a one-way valve and pipeline.    USE - Household kitchen garbage processor used for decomposing kitchen garbage into organic fertilizer (claimed).    ADVANTAGE - The household kitchen garbage processor is economic and convenient to use, and ensures less space requirement and no environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of household kitchen garbage processor.    Bucket groove (10)    Vacuum device (20)    Deodorization pool (30)    Seal cover (40)    Power device (50)
NOVELTY - Method for preparing organic matrix involves selecting and pre-processing selected raw materials, fermenting the resulting processed raw materials, drying fermented mixture and subjecting the dried mixture to exhaust gas treatment to obtain product.    USE - The method is useful for preparing organic matrix (claimed).    ADVANTAGE - The method is environmentally-friendly, cost-effective and less labor-intensive.
NOVELTY - The furnace has a furnace part provided with an upper furnace body (6) and a lower furnace body (13), where the upper furnace body is mounted with a top end of a furnace cover (5). A feeding device is mounted with the furnace cover. A side wall of the furnace body is mounted with first, second and third air inlets (7,8,9). The lower furnace body is equipped with a gas outlet (12) and mounted with an ash pan (15), where the ash pan is mounted with a spiral conveying machine (16). The feeding device is provided with a pneumatic gate (4) that is connected with a transition hopper (3).    USE - Biomass multi-fire layer gasification furnace.    ADVANTAGE - The furnace body is connected with the air inlets, where the furnace body is arranged with a multi-fire layer so as to increase production efficiency of the furnace body.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass multi-fire layer gasification furnace.    Transition hopper (3)    Pneumatic gate (4)    Furnace cover (5)    Upper furnace body (6)    Air inlets (7,8,9)    Gas outlet (12)    Lower furnace body (13)    Ash pan (15)    Spiral conveying machine (16)
NOVELTY - Preparation of biomass granule fuel comprises mixing raw materials comprising 4 pts. wt. wood powder or sawdust, 0.8-1.2 pts. wt. sorghum shell, and 0.5-1 pt. wt. crushed corn straw, crushing rice corn material to 3-5 cm, adding 0.009-0.012 times lime, and mixing; molding and extruding at 150-220 degrees C, where rotating speed is 750-1000 revolutions/minute; sieving to length of 2-6 cm and diameter of 6-8 mm; and cooling and filling.    USE - Method for preparing biomass granule fuel (claimed).    ADVANTAGE - The fuel can absorb water, reduces moisture biomass particles, has high sugar content of sorghum shell, extends burning time, utilizes full heat, and has good combustion effect, low biomass granule fuel ash, low moisture content, easy ignition, calorific value of 4500-5200 kcal, and thermal efficiency of more than 95%.
NOVELTY - Method for producing biogas from organic waste, involves using specially designed container, organic waste tank and heavy leak proof pipes, decaying organic waste to generate methane gas, and storing methane gas in highly insulated container, where the method involves allowing the organic waste to decay in the container, and conversion of the organic waste into biogas.    USE - The method is useful for producing biogas from organic waste, where the biogas is methane gas which is used for cooking purpose (all claimed).    ADVANTAGE - The method reduces pollution, and avoids chance of fire accidents.
NOVELTY - The method involves fixing transgenic rice seed and parent sample in the stage. All-solid-state semiconductor laser is used for illuminating laser to the transgenic rice seed and parent sample. The Raman detection device is used for obtaining Raman spectrum information of transgenic rice and its parent. The Raman spectrum map of the sample is drawn in high-dimensional characteristic space, by analyzing the Raman spectrum information, so as to estimate the transgenic rice seed sample category.    USE - Method for rapid detection of transgenic rice seed and its parent.    ADVANTAGE - The rapid detection of transgenic rice seed and its parent can be performed easily and efficiently, without polluting the environment. The detection cost can be reduced. The recognition precision of transgenic rice seed and its parent can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for rapid detection of transgenic rice seed and its parent.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram explaining the process for rapid detection of transgenic rice seed and its parent. (Drawing includes non-English language text)
NOVELTY - Biological modifier comprises fermentation liquid (A) comprising Acremonium persicinum (CCTCC M 2013200), fermentation liquid (B) comprising Azotobacter chroococcum (CGMCC 1.2391), fermentation liquid (C) comprising Paenibacillus mucilaginosus (CGMCC 1.2326), fermentation liquid (D) comprising Bacillus megaterium (CGMCC 1.1870), fermentation liquid (E) comprising B.megaterium (CGMCC 1.813), and microelement mixed solution. The microelement mixed solution contains zinc sulfate, manganese sulfate and ammonium citrate.    USE - The biological modifier is useful in soil for cultivation of tomato in greenhouse (claimed).    ADVANTAGE - The biological modifier provides effect for a long period of time, prevents disease of tomato, and improves quality of tomato.    DETAILED DESCRIPTION - Biological modifier comprises 40-50 ml fermentation liquid (A) as each ml of fermentation liquid (A) comprises 8x 106 cells of Acremonium persicinum (CCTCC M 2013200), 5-10 ml fermentation liquid (B) as each ml of fermentation liquid (B) comprises 3.5x 108 colony-forming units (CFU) of Azotobacter chroococcum (CGMCC 1.2391), 10-15 ml fermentation liquid (C) as each ml of fermentation liquid (C) comprises 4.5x 108 CFU/ml Paenibacillus mucilaginosus (CGMCC 1.2326), 10-15 ml fermentation liquid (D) as each ml of fermentation liquid (D) comprises 5.4x 108 CFU/ml Bacillus megaterium (CGMCC 1.1870), 5-10 ml fermentation liquid (E) as each ml of fermentation liquid (E) comprises 4.8x 108 CFU/ml B.megaterium (CGMCC 1.813), and 5-10 ml microelement mixed solution. Each 1000 ml microelement mixed solution comprises 5-10 g zinc sulfate, 5-10 g manganese sulfate, 1-5 g ammonium citrate, 5-10 g ferrous sulfate, 1-10 ml phosphoric acid having concentration of 85 wt.%, 1-20 g chitooligosaccharide and water (remainder).
NOVELTY - Wood tar efficient production system comprises conversion furnace body (D), liquid storage tank (8), inner furnace body (4), gasification room (23), outside furnace body (7), furnace middle layer, focus room, cooling water layer, wood tar outlet, drain pipe, discharge pipe, air compressor, pressure valve, exhaust valve, air inlet, blast pipe, wind pipe, and blower.    USE - Wood tar efficient production system used for producing combustible gas.    ADVANTAGE - The method uses pressed branches, wood chips, wheat straw, and corn stalk as raw materials. The production system is highly efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wood tar efficient production system.    Inner furnace body (4)    Outside furnace body (7)    Liquid storage tank (8)    Gasification room (23)    Conversion furnace body (D)
NOVELTY - The method involves carrying out combustion reaction of a portion of a biomass raw material and oxygen. The biomass granule raw material is subjected to heat decomposing reaction under anoxic condition. The volatile portion and coke are separated. The coke and fine dust are purified in the mixing gasification furnace (1). The tar is mixed with the gas through cyclone separator (2). The fine coke and tar are mixed with spray water through spray tower (3). An activated carbon granule (5) is absorbed with the mixed gas through dust collector.    USE - Method for gasifying biomass granule used for producing electric power energy.    ADVANTAGE - The dust-removing effect for gasifying the biomass granule is improved. The resources needed for gasifying the biomass granule is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the process for gasifying biomass granule used for producing electric power energy.    Mixing gasification furnace (1)    Cyclone separator (2)    Spray tower (3)    Activated carbon granule (5)
NOVELTY - Protein, comprising either: (i) fully defined 719 amino acids (SEQ ID NO: 2) as given in the specification; or (ii) a sequence obtained by substituting, deleting and/or adding at least one amino acid residue to SEQ ID NO: 2 having same function, is new.    USE - The protein is useful for immobilizing beta -xylosidase, alpha -arabinosidase or beta -glucosidase and degrading biomass, preferably corn cob. The DNA, expression cassette, recombinant vector, recombinant strain and transgenic cell line are useful in preparing beta -xylosidase, alpha -arabinosidase or beta -glucosidase and (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) DNA molecule encoding the protein; and    (2) expression cassette, recombinant vector, recombinant strain or transgenic cell line comprising the DNA molecule;    (3) use of the protein, comprising immobilizing beta -xylosidase, alpha -arabinosidase or beta -glucosidase at optimum pH of 4.5 and optimum temperature of 60 degrees C; and    (4) preparing the beta -xylosidase, alpha -arabinosidase or beta -glucosidase, comprising fermenting the recombinant bacteria to obtain beta -xylosidase, alpha -arabinosidase or beta -glucosidase.
NOVELTY - Method of preparing organic fertilizer, involves obtaining 1 pt. wt. leavening agent and 5-10 pts. wt. corn powder or wheat bran, uniformly drying the materials, diluting the strain, uniformly mixing a sludge and plant straw, spraying the mixed strain and fermenting the mixture at 50-60 degrees C for 48 hours.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly, increases utilization rate of plant straw and reduces the usage of chemical organic fertilizer.
NOVELTY - Complex microbial sclerotia comprises 10-15 pts. cellulase, 15-18 pts. lignin catalase, 9.5-16 pts. xylanase, 0.5-3 pts. 5% alkali, 12-20 pts. Lactobacillus, 10-25 pts. Bacillus, 8-16 pts. Bacillus pumilus, 35-50 pts. active enzyme and 200-300 pts. phytic acid.    USE - The complex microbial sclerotia is useful for decomposing straw (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the complex microbial sclerotia, comprising: mixing the above raw materials and granulating in a round transformation granulator.
NOVELTY - The fermentation and processing method of sheep manure involves: adding 2-8 times by weight of water to sheep manure containing impurities, mixing uniformly; crushing straw into granules, adding fermentation agents and water and mixing well; and mixing treated sheep manure, impurities and straw mixture, covering with plastic film and fermenting in unventilated condition at room temperature for 10-20 days, opening film and sprinkling with cornmeal mixed with bacteria on the surface, closing the plastic film and fermenting for 10-20 days.    USE - Fermentation and processing of sheep manure, which is useful as fertilizer.    ADVANTAGE - The method enables simple, economical, environmentally-friendly processing of sheep manure that improves soil quality and provides nutrients for long time with reduced burning phenomenon.    DETAILED DESCRIPTION - The fermentation and processing method of sheep manure involves: adding 2-8 times by weight of water to sheep manure containing impurities, mixing uniformly; crushing straw into granules, adding fermentation agents and water and mixing well; mixing treated sheep manure, impurities and straw mixture, covering with plastic film and fermenting in unventilated condition at room temperature for 10-20 days, opening film and sprinkling with cornmeal mixed with bacteria on the surface, closing the plastic film and fermenting for 10-20 days, then normal-fermenting at a temperature of 38-45 degrees C, and finally deep-fermenting at a temperature of 80-90 degrees C; and deodorizing the mixture, adding 1-2 times by weight of water into plastic bags and sealing plastic bag. The straw pellets, fermentation agents and water are added in a weight ratio of 100:1:30. The treated sheep manure containing impurities and straw are mixed in a weight ratio of 1-2:1-2.
NOVELTY - Method of preparing organic fertilizer, involves pre-processing the agricultural waste and crushing into 50-70 meshes sieve powder, regulating the water content to 30-40%, inoculating strain into the crushed material, fermenting the mixture at room temperature for 3-5 days and then granulating the fermented mixture to obtain the finished product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The fertilizer is rich in nutrients and convenient to use.
NOVELTY - Preparing fertilizer using crop straw comprises (i) spraying crop straw on fermentation culture solution, and soaking in water for 24-36 hours; (ii) paving a first sludge layer on ground floor of the fermentation tank, where thickness is 10-20 cm; (iv) paving a first layer of 60% crop rice, and spraying lime water (small amount); (iv) paving a second layer of 30% fine soil and a third layer of 10% animal manure, and covering outer layer with mud-free air permeable cover; and (v) turning once for 5-10 days, spraying the fermentation culture liquid, and covering the outer layer for 5-10 days.    USE - The method is useful for preparing fertilizer using crop straw (claimed).    ADVANTAGE - The method: utilizes waste straw; reduces the compost period and turning times; rarely allows the nutrition element loss; and utilizes the crop straw component having maximum effect.    DETAILED DESCRIPTION - Preparing fertilizer using crop straw comprises (i) spraying crop straw on fermentation culture solution, and soaking in water for 24-36 hours; (ii) paving a first sludge layer on ground floor of the fermentation tank, where thickness is 10-20 cm; (iv) paving a first layer of 60% crop rice, and spraying lime water (small amount); (iv) paving a second layer of 30% fine soil and a third layer of 10% animal manure, and covering outer layer with mud-free air permeable cover; and (v) turning once for 5-10 days, spraying the fermentation culture liquid, and covering the outer layer for 5-10 days, where the fertilizer comprises 60% crop straw, 10% animal manure, and 30% fine soil.
NOVELTY - Method of preparing biological organic fertilizer, involves obtaining 10 pts. wt. soybean meal, 10 pts. wt. peanut and 20 pts. wt. gas-liquid, mixing the raw materials to obtain uniform mixture, fermenting the material for 50-60 days to obtain the organic fertilizer, drying the organic fertilizer material until the water content is less than 10-12% at 60 degrees C and packaging the finished product.    USE - As fertilizer.    ADVANTAGE - The fertilizer improves soil fertility, preferably increases nitrogen source in soil, enhances plant disease resistance and drought resistance ability, increases the absorbability of water, reduces the usage amount of chemical fertilizer and increases the quality of crops, and is prepared cost-effectively.
NOVELTY - The device has a smashing device (2), a screening device (4) and a material conveying device (6). The material conveying device is equipped with a continuous material adding device (5). The material conveying device is equipped with a belt-type conveying machine. The feeding cabin is matched with the first feeding device (1). The smashing device and the screening device are matched with the second feeding device (3).    USE - Online quantitative adding device for adding organic fertilizer biological microbial inoculum.    ADVANTAGE - The adding efficiency is improved. The device cost and investment cost are reduced. The cost of organic biological fertilizer is achieved. The wastage of biological agent is avoided, and the production cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the online quantitative adding device for adding organic fertilizer biological microbial inoculum.    Feeding devices (1,3)    Smashing device (2)    Screening device (4)    Continuous material adding device (5)    Material conveying device (6)
NOVELTY - A ventilation-type floor energy-saving fermentation device comprises fermentation tunnel (3), rolling door (1), air outlet pipe (5), solar energy solar panels (2), charging electric discharge circuit (7), storage battery (12), heater (8), heat exchanger (6), high-pressure fan (4), waste gas filtering tank (13), biological bed (14) and ventilation-type floor (9).    USE - Ventilation-type floor energy-saving fermentation device.    ADVANTAGE - The device has uniform aerobic fermentation, stable product quality, low operation energy consumption and low cost. It removes odor of gas in waste gas, thus it is environment-friendly. The fermentation tunnel has rectangular brick-concrete structure building.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of ventilation-type floor energy-saving fermentation device.    Rolling door (1)    Solar energy solar panels (2)    Fermentation tunnel (3)    High-pressure fan (4)    Air outlet pipe (5)    Heat exchanger (6)    Charging electric discharge circuit (7)    Heater (8)    Ventilation-type floor (9)    Storage battery (12)    Waste gas filtering tank (13)    Biological bed (14)
NOVELTY - The fermentation pool (3) has a rubber film (2), an insulation quilt (1), an air outlet pipe (5), a heat exchanger (10), a high pressure fan (6), a waste gas filtering pool (11), a biological bed (12), and a ventilation hole (8). The air outlet pipe is provided on the upper portion of the fermentation pool wall portion. The heat exchanger is connected to high pressure fan and waste gas filtering pool. The waste gas filtering pool is connected to the biological bed.    USE - Floor type ventilation fluorescent solid waste aerobic fermentation pool for forming livestock manure used in agricultural field.    ADVANTAGE - The solid waste material fermentation is performed uniformly. The stable quality of the fermenting product is ensured. Energy consumption and operation cost of the fermentation pool are reduced. The odor in the waste gas is removed effectively and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the floor type ventilation fluorescent fermentation pool.    Insulation quilt (1)    Rubber film (2)    Fermentation pool (3)    Air outlet pipe (5)    High pressure fan (6)    Ventilation hole (8)    Heat exchanger (10)    Waste gas filtering pool (11)    Biological bed (12)
NOVELTY - The pH value adjusting device has fermentation groove (1) whose top portion is matched with groove cover (101). The groove cover is provided with motor (103). The water flows into water washing tower (2) that is connected to washing water connecting pipe. A purification pipe (a2) is connected to one end of wooden interior shoulder room (3) while another end is connected to one end of marsh gas pipe (a3) and another end is connected to purification fan (301). Other end of purification fan is connected to marsh gas tank (4).    USE - Device for adjusting pH value of closeness fermentation organic fertilizer.    ADVANTAGE - The pH value of the fermenting groove is adjusted effectively. The aerobic optimum fermentation environment is provided, so that the pH value in fermentation groove is equal at entire location.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for adjusting pH value of closeness fermentation organic fertilizer.    Fermentation groove (1)    Water washing tower (2)    Wooden interior shoulder room (3)    Marsh gas tank (4)    Groove cover (101)    Motor (103)    Purification fan (301)    Purification pipe (a2)    Marsh gas pipe (a3)
NOVELTY - High nitrogen content tea fertilizer comprises 50-60 wt.% biological organic fertilizer, 40-50 wt.% amino acid fertilizer, and 3 wt.% magnesium stearate. The biological organic fertilizer comprises nitrogen, phosphorus pentoxide and potassium oxide at a ratio of 4:1:1.1.    USE - High nitrogen content tea fertilizer used for increasing stress resistance of tea tree.    ADVANTAGE - The fertilizer has more than 5-6% nitrogen content, meets the microelement demand, and improves yield and quality of tea.    DETAILED DESCRIPTION - High nitrogen content tea fertilizer comprises 50-60 wt.% biological organic fertilizer, 40-50 wt.% amino acid fertilizer, and 3 wt.% magnesium stearate. The biological organic fertilizer comprises nitrogen, phosphorus pentoxide and potassium oxide at a ratio of 4:1:1.1. The biological organic fertilizer is prepared by taking 70% chicken manure, 20% mushroom residue, 9.7% reed powder, and 0.3% fermentation strain, keeping water content to 40-45%, uniformly mixing, and stacking at 60-65 degrees C to obtain a high-quality biological organic fertilizer having nitrogen, phosphorus, and potassium total nutrient content of more than 8%, where nitrogen content is 4.5 wt.%, phosphorus content is 2.5 wt.%, potassium content is 1.8 wt.%, organic matter content is greater than or equal to 75 wt.%, effective viable cells is greater than or equal to 5000 million/g, water content is 30 wt.%, and pH is 6.5. The raw material amino acid is an amino acid fertilizer extract scraps added with ash solidification treatment from biological plant.
NOVELTY - A fully water-soluble solid biological organic fertilizer is produced by carrying out yeast fermentation of wastewater to generate nutrient-rich wastewater; concentrating the wastewater to obtain semifluid; flash drying the semifluid to obtain powder; and supplementing nitrogen-phosphorus-potassium nutrient agent in the powder, and adding plant rhizosphere-promoting microbial inoculum.    USE - Method for producing fully water-soluble solid biological organic fertilizer (claimed) used in promoting plant growth and formation of dominant flora, and inhibiting pathogens.
NOVELTY - A radix scrophulariae compound fertilizer contains an organic base fertilizer and an inorganic fertilizer. The fertilizer further contains combination agent containing Bacillus subtilis, Trichoderma harzianum and Trichoderma reesei, and has a viable count of 500-800 million/g.    USE - Radix scrophulariae compound fertilizer is useful for Wuling mountain area and acid soils (claimed).    ADVANTAGE - The radix scrophulariae compound fertilizer has high nutritional value, can be prepared with high yield and quality, can improve pH of soil, and increase diversity of soil microbial community.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of radix scrophulariae compound fertilizer, involving adding animal excrement to poultry manure, uniformly mixing, composting the mixture and then fermenting for 10-14 days, adding organic base fertilizer to the mixture and then drying, adding quicklime, inorganic fertilizer and combination agent to the mixture, and stirring; and    (2) use of radix scrophulariae compound fertilizer for Wuling mountain area and acid soils.
NOVELTY - Lily fertilizer comprises 20-30 mass% active biological fertilizer, 5-10 mass% humic acid, 0.1-5 mass% trace elements, and 60-70 mass% inorganic fertilizer. The active biological fertilizer comprises 40-50 wt.% vegetable, 10-20 wt.% soybean meal, 30-40 wt.% chicken manure, 10-20 wt.% tobacco, and 0.5-1 wt.% Effective Microorganisms (EM) composite liquid. The trace elements comprise magnesium, boron, zinc magnesium sulfate, borax, or zinc sulfate. The inorganic fertilizer comprises 20-40 wt.% urea, 15-25 wt.% monoammonium phosphate, 20-40 wt.% potassium sulfate, and 15-25 wt.% ammonium sulfate.    USE - Lily fertilizer.    ADVANTAGE - The fertilizer is quick acting fertilizer, has balanced nutrition, and can increase yield and quality of lily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising adding biological fertilizer raw materials, adjusting water control to 50-60%, adding alkaline to regulate pH value to 7-9, then uniformly stirring and mixing, carrying out aerobic fermentation to obtain the activated biological fertilizer; and adding biological fertilizer, humic acid, trace elements and inorganic fertilizer, crushing, uniformly mixing, metering and packaging.
NOVELTY - Organic fertilizer comprises 100-180 pts. wt. mixture of neem leaves, camphor leaves, quinquefolia and cattle komarovii, and 200-400 pts. wt. mixture of cow dung, biogas and corn stover.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is environment-friendly, and kills insect and pathogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) drying and crushing neem leaves, camphor leaves, quinquefolia and cattle komarovii in pulverizer to obtain mixture;    (B) fermenting mixture of cow dung, biogas and corn stover at 28-32 degrees C for 15-20 days;    (C) mixing fermented mixture with former mixture; and    (D) drying and granulating obtained mixture to obtain product as powder or granule.
NOVELTY - Bio-organic fertilizer comprises 12-15% nitrogen, phosphorus pentoxide and potassium oxide (in weight ratio of 6:0-2:5-7), 60-75% organic substance having effective viable count of 0.5-1 hundred million/g, 30% water and 0.2-0.3% nicotine powder having 20-40 meshes particle. The pH of fertilizer is 6.0-7.0.    USE - Bio-organic fertilizer used for suppressing soil-borne pests (claimed) and preventing and treating plant diseases and insect pest.    ADVANTAGE - The bio-organic fertilizer improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) crushing tobacco stalk and rice bran;    (B) fermenting crushed materials with micro-organism and water to obtain fermented material;    (C) stirring fermented material and functional micro-organism; and    (D) crushing and sieving obtained mixture to obtain powder as product that is packed.
NOVELTY - Extracting and purifying emodin comprises extracting Polygonum cuspidatum resveratrol by-product with ethyl acetate, discarding precipitate to obtain extract, adding alkaline solution, extracting, adding potassium chloride saturated solution, stratifying, and combining alkaline solution layer; and adding acidic solution, filtering, collecting precipitate, washing with deionized water to obtain crude emodin, crystallizing with organic solvent, and evaporating to dryness.    USE - Method for extracting and purifying emodin (claimed).    ADVANTAGE - The method increases added value of Polygonum cuspidatum resources, promotes development and utilization of Polygonum cuspidatum resources, helps protect the environment, and increases corporate profits.
NOVELTY - Preparation of 3-halo-2-methylaminobenzoic acid comprises taking o-haloaniline, chloral hydrate, hydroxylamine hydrochloride, sodium sulfate and 2 mol/L hydrochloric acid, condensing, adding sulfuric acid, performing cyclization, adding organic solvent and acid binding agent, performing methylation, adding alkali and oxidant, reacting, extracting with organic solvent, acidifying until pH is 4-6, crystallizing, filtering and drying.    USE - Method for preparing 3-halo-2-methylaminobenzoic acid (claimed).    ADVANTAGE - The method is simple, stable and environment-friendly, and has inexpensive and readily available raw materials and high yield and purity.
NOVELTY - Preparation of aprepitant intermediate comprises taking (2R)-4-benzyl-2-((1R)-1-(3,5-bis(trifluoromethyl)phenyl)ethoxy)morpholin-3-one and carrying out crystallization-induced configuration transformation using ether-tetrahydrocannabinol system.    USE - Method for preparing aprepitant intermediate (claimed).    ADVANTAGE - The method is short and environment-friendly and has low production cost, high productivity and high atomic utilization rate.
NOVELTY - A modular device comprises a shredding system, biomass composition, a digester, a fermentation chamber, a biogas tank, a chamber, a drainage system and a combined heat and electricity generation unit, where the biomass composition is filled in the digester, the fermentation chamber and the biogas tank and the combined heat and electricity generation unit generates 8-12 kW of power.    USE - Modular device for use in methane fermentation of organic waste of plant origin and animal origin.
NOVELTY - Preparing pesticide involves utilizing chlorothalonil, garlic oil, radix sophorae flavescentis, fructus cnidii, sodium carboxymethyl cellulose, sulfur, lignin and modified starch powder. Lignin is mixed with water to obtain 10% of lignin solution. Modified starch is added uniformly in lignin solution, stirred and then sulfur, garlic oil, chlorothalonil, fructus cnidii fruit aqueous extract and radix sophorae flavescent aqueous extract are mixed to obtain a product. Sodium carboxymethyl cellulose is dissolved with product to obtain pesticide.    USE - Method for preparing pesticide (claimed).    ADVANTAGE - The method is simple, enables to prepare eco-friendly pesticide that is easy to use.
NOVELTY - Bio-pesticide comprises 35-46 pts. Alternaria cyclosporine, 20-40 pts. jasmine oil, 12-18 pts. rice hull powder, 21-26 pts. amino acid, 5-12 pts. allicin, 5.5-7 pts. magnesium phosphate, 5-8 pts. star anise, 35-46 pts. corn straw, 10-16 pts. Verticillium powder, 5-19 pts. amino oligosaccharin, 25-40 pts. tung wood meal and 80-100 pts. water.    USE - Used as bio-pesticide.    ADVANTAGE - The bio-pesticide does not produce pesticidal residue (claimed), is safe and economical.
NOVELTY - Plant for generating biogas from biomass obtained from kitchen waste from hotels, messes or canteens, comprises: an anaerobic digester (6) in the form of a closed chamber having a hopper (2) at the top; an outlet leading to a gas holding tank (20), an outlet for removing sludge; mechanized stirrer having a vertical shaft, where the vertical shaft has two propellers (11) one at the tapper level to mix and push the contents downwards while the other propeller to stir and push the sludge upwards; and predigester (24) compartment with a slopping platform at the bottom.    USE - The plant is useful for generating biogas from biomass obtained from kitchen waste from hotels, messes or canteens.    ADVANTAGE - The plant: avoids the use of special storages like cold rooms, thus avoiding the extra expenditure; provides additional unconventional source of energy; and eliminates the formation of scum.    DETAILED DESCRIPTION - Plant for generating biogas from biomass obtained from kitchen waste from hotels, messes or canteens, comprises: an anaerobic digester (6) in the form of a closed chamber having a hopper (2) at the top of the chamber; an outlet for biogas leading to a gas holding tank (20), an outlet for removing sludge; at the top, a mechanized stirrer having a vertical shaft reaching downwards, the vertical shaft having two propellers (11) one at the tapper level to mix and push the contents downwards while the other propeller is located at the lower level to stir the contents and push the sludge upwards; and a predigester (24) compartment with a slopping platform at the bottom and further having many wide openings. The hopper and predigester are located in a way so that the major portion of the predigester remains dipped in the liquid contents of the anaerobic digester.    DESCRIPTION OF DRAWING(S) - The figure illustrates the biogas plant.    Hopper (2)    Anaerobic digester (6)    Propellers (11)    Gas holding tank (20)    Predigester (24)
NOVELTY - Invention relates to the catalytic conversion of a renewable raw material - products of the biomass fermentation (ethanol, fusel alcohols) and their mixtures with vegetable oil into an alkane-aromatic fraction C3-C11+, which can be used for obtaining fuel components. The method of obtaining alkane and aromatic hydrocarbons from the products of the biomass processing for obtaining the hydrocarbon fuel components includes passing the products of the biomass processing through a layer of a preliminarily regenerated zeolite ZSM-based catalyst, containing Pd and Zn, in an inert atmosphere at an increased temperature. The method is characterised by the fact that as the catalyst used is the Pd-Zn/ZSM/Al2O3 catalyst of the general formula of 0.6 wt % Pd-1 Zn/Al2O3/ZSM, with the products of the biomass processing, which contain a mixture of organic fermentation products or fusel alcohols, being passed through the catalyst layer at a temperature of 280-500 degrees C and volume rate of 0.3-6 h-1.    USE - Chemistry.    ADVANTAGE - Extension of the raw material base and method for obtaining alkane and aromatic hydrocarbons.5 cl, 6 tbl, 26 ex
NOVELTY - Microorganism-enriched fertilizer comprises 80-90 pts. wt. animal manure, 4-9 pts. wt. sodium dihydrogen phosphate, 1-3 pts. wt. raspberry, 9-12 pts. wt. limonitum, 4-10 pts. wt. cedar wood chips, 5-8 pts. wt. wood powder, 0.01-0.02 pt. wt. Bacillus cereus powder, 0.01-0.02 pt. wt. Bacillus thuringiensis powder, 3-6 pts. wt. potassium mineral powder, 11-16 pts. wt. stone powder, 4-6 pts. wt. diammonium phosphate, 6-15 pts. wt. sodium tripolyphosphate, and 0.01-0.02 pt. wt. rhizobium powder.    USE - Microorganism-enriched fertilizer is used for soil.    ADVANTAGE - The microorganism-enriched fertilizer has long-lasting effect, and is rich in nutrients. The fertilizer improves the content of organic substances in soil.
NOVELTY - The method involves performing heating passivation of a high voltage system. A synthesis column is filled to a stripper U-shaped tube at 8min-12min. The pressure of the high voltage system is raised to 3.0 MpaG. A pressure control valve of high voltage system is opened, when an ammonia synthesis tower reaches a top of a reactor. A stripper level control valve in a liquid stripper is opened. The investment rate of carbon dioxide in the stripper is improved.    USE - Low-voltage discharge urea production method.    ADVANTAGE - The gas phase emptying of environment pollute and cause resource waste is effective prevented, and the operating time is saved.
NOVELTY - Composition comprises 0.4-15 pts. wt. fluorine-modified nickel-containing hydrotalcite, 0.002-0.25 pts. wt. silane couple agent, 49.5-985 pts. wt. lubricant, 4000-90000 pts. wt. 2,3,3,3-tetrafluoropropene, 0-60000 pts. wt. fluoroethane, 0-15000 pts. wt. 1,1-difluoroethane, 0-5000 pts. wt. isobutane, and 0.8-1 pts. wt. 3-methyl-1-propylpyridinium bis(trifluormethylsulfonyl)imide.    USE - Used as a composition containing tetrafluoropropene.    ADVANTAGE - The composition has good lubricant compatibility (claimed) and flame retardancy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the composition, comprising (a) dispersing fluorine-modified nickel-containing hydrotalcite in 1000 pts. wt. ethanol, thn adding silane coupling agent, reacting at 25 degrees C for 10-20 hours, removing the ethanol by filtration process, adding the lubricant, and reacting at 25 degrees C for 10-20 hours to obtain nano lubricant; and (b) adding the nano lubricant with the 2,3,3,3-tetrafluoropropene, fluoroethane, 1,1-difluoroethane, isobutane and 3-methyl-1-propylpyridinium bis(trifluormethylsulfonyl)imide, pre-mixing at -45 degrees C to -60 degrees C for 10-35 hours under liqud-state, added to the high flux micro-channel glass reactor under flow rate of 10-100 Kg/hours to obtain mixed product.
NOVELTY - A powdered or granular organic-inorganic hybrid fertilizer is obtained by directly mixing sugarcane filter mud and dry-processed filter mud or conditioning agents, controlling pH value to 6-7, reacting mixture and optionally stacking.    USE - Powdered or granular organic-inorganic hybrid fertilizer (claimed).    ADVANTAGE - The powdered or granular organic-inorganic hybrid fertilizer is environmentally-friendly, in-situ-treated and economically prepared.
NOVELTY - Fertilizer composition comprises 18-20 pts. wt. nitrogenous fertilizer, 19-21 pts. wt. phosphate fertilizer, 25-27 pts. wt. potash fertilizer, 80-100 pts. wt. dairy manure, 70-90 pts. wt. sheep manure, 20-30 pts. wt. rock phosphate, 30-40 pts. wt. potassium mineral powder, 40-60 pts. wt. lees, 2-4 pts. wt. leavening agent, 2-3 pts. wt. Borax (RTM: Sodium tetraborate), 40-50 pts. wt. flour, 20-30 pts. wt. mulberry leaves and 160-200 pts. wt. water.    USE - Fertilizer composition used for cultivating maple tree (claimed).    ADVANTAGE - The fertilizer composition is prepared in eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a composition, which involves:    (A) mixing crushed raw materials with water, and then stirring them;    (B) sealing the obtained material for 3-5 days, and then keeping for 12 hours; and    (C) granulating the obtained material to obtain the finished product.
NOVELTY - Synthesis method of ganirelix involves (a) conjugating N-terminal protective groups with D-alanine using condensation agent and an activating agent and conjugating an amino-protecting group with an amino resin, and esterifying to obtain a peptide resin, and (b) performing removal of amino-protecting group and coupling reaction in peptide resin from N-terminal to C-terminal end using condensation agent and an activating agent to obtain ganirelix resin, then carrying out acidolysis, and purifying crude product to obtain purified ganirelix.    USE - The method is useful for synthesizing ganirelix (claimed).    ADVANTAGE - The method increases purity and yield of ganirelix without damaging environment.    DETAILED DESCRIPTION - Synthesis method of ganirelix involves (a) conjugating N-terminal protective groups with D-alanine using condensation agent and an activating agent and conjugating an amino-protecting group with an amino resin, and esterifying to obtain peptide resin, and (b) coupling the remaining protected amino acid in peptide resin from N-terminal to C-terminal end using condensation agent and an activating agent to obtain ganirelix resin, then carrying out acidolysis, purifying crude product to obtain purified ganirelix, where the acidolysis step uses acid solution comprising 80-95 vol.% trifluoroacetic acid, 1-10 vol.% EDTA, and water (remainder).
NOVELTY - The furnace has furnace casing formed of heat preservation material, and arranged with angle-shaped box having air inlet. The casing bottom surface is arranged with discharging port. The casing inner portion is set with pulling motor that is connected with shifting material array umbrella by hollow shaft. An inner water pipe is connected with water spray pump (17-2) by soft joint for cooling carbonized product. The upper portion of furnace casing is set with combustion temperature setting unit and lower portion of furnace casing is set with carbonization temperature setting unit.    USE - Straw carbonization furnace used in agricultural field.    ADVANTAGE - The straw carbonization furnace is provided with uniform carbonization effect, reduced pollution to environment, reduced solid carbon emission effect and increased soil fertility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw carbonization furnace. (Drawing includes non-English language text)    Operation platform (4)    Discharge pipe (13)    Washing tower (14)    Suction machine (15)    Water spray pump (17-2)
NOVELTY - Synthesis of 4-chromone derivative involves reacting phenolic compound (I) and alkyne compound (II) in absence of solvent to obtain benzyl compound (III) as intermediate, and then subjecting the resultant product to intramolecular cyclization process in presence of catalyst to obtain 4-chromone derivative (IV). The catalyst comprises polyphthalamide, concentrated sulfuric acid, diphenyl ether, and/or Eaton reagent.    USE - Synthesis of 4-chromone derivative (claimed).    ADVANTAGE - The method provides 4-chromone derivative by environmentally-friendly, economical and simple process with high yield.    DETAILED DESCRIPTION - Synthesis of 4-chromone derivative involves reacting phenolic compound of formula (I) and alkyne compound of formula (II) in absence of solvent to obtain benzyl compound of formula (III) as intermediate compound, and then subjecting the resultant product to intramolecular cyclization process in presence of catalyst to obtain 4-chromone derivative of formula (IV). The catalyst comprises polyphthalamide, concentrated sulfuric acid, diphenyl ether, and/or Eaton reagent.    R1-R4=H, halo, methoxy, trifluoromethyl, nitro, alkyl or aryl;    R5=H, ester group, alkyl or aryl;and    R6=alkyl.
NOVELTY - This new utility model claims of one of methyl alcohol water hydrogen generation system, comprising methyl alcohol water storage container, transport pump, methanol hydrogen production system, fuel cell, water circulation cooling system and heat pump device, wherein the methyl alcohol water storage container, used for storage water raw material methyl alcohol, the methyl alcohol raw material can lower water in driving the transporting pump, transport pipe by transporting to the methanol hydrogen production system, methanol hydrogen system of water, methyl alcohol and water for generating reforming reaction prepared hydrogen, and for providing hydrogen to fuel cell, fuel cell, hydrogen and oxygen for generating electrochemical reaction producing electric energy, water circulation cooling system, used for fuel battery to carry out cooling heat abstractor of heat pump device, can absorb water circulation cool and heat and warm water in system, transformation as high temperature heat source, and for transporting pipe in the methyl alcohol raw material heating water. This new utility model can make fuel battery work steady, strong reliability, and can full utilize fuel cell of generation of heat.
NOVELTY - The array (10) has artificial-photosynthesis modules (12) that contain electrolysis chamber for hydrogen (14) and electrolysis chamber for oxygen (16) which are isolated so that hydrogen and oxygen gases are generated and are not mixed. The module inclines in a direction in which hydrogen gas generation unit and oxygen gas production unit of another artificial-photosynthesis module are located in a line. Electrolyte aqueous solution is supplied to electrolysis chamber for hydrogen and electrolysis chamber for oxygen of each artificial-photosynthesis module by preset flow volume.    USE - Artificial-photosynthesis array.    ADVANTAGE - The artificial-photosynthesis array suppresses mixing of hydrogen gas and oxygen gas, and maintains the ion concentration or pH value in water constantly by devising the connection form of artificial-photosynthesis modules.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the artificial-photosynthesis array.    Artificial-photosynthesis array (10)    Artificial-photosynthesis module (12)    Container (13)    Electrolysis chamber for hydrogen (14)    Electrolysis chamber for oxygen (16)
NOVELTY - The system has electrolyte cell in which hydrogen gas and oxygen gas are produced with the electric power obtained in photoelectric conversion unit, and is provided with gas-evolution electrode which electrolyzes the electrolyte aqueous solution. The photoelectric conversion unit and electrolyte cell are electrically connected in series. The photoelectric conversion unit or the electrolyte cell is located in each end in an arrangement state.    USE - Electrolysis system of water.    ADVANTAGE - The adjustment of the voltage concerning an electrolysis chamber cell is attained, and the loss of the over-voltage which electrolysis of water requires is decreased. The immersion of electrolyte aqueous solution is made unnecessarily, by dividing a photoelectric conversion unit and a gas-evolution electrode, so that the performance decrement by immersion is avoided. The hydrogen is manufactured at low cost. The water is electrolyzed and hydrogen gas and oxygen gas are obtained in an electrolysis chamber cell, so that the area of an electrolysis chamber is made smaller.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis system of the water. (Drawing includes non-English language text)    Electrolysis system of water (10)    Photoelectric conversion unit (12)    Electrolyte cell (14)    Hydrogen gas collection unit (20)    Oxygen gas recovery unit (22)
NOVELTY - A laminar biocarrier for wastewater treatment in the form of elastic, flexible and resistant mesh, where the fabric is made from yarn interlacing or lignocellulosic material and supports and immobilizes a layer of fungal biomass wood rot.    USE - The laminar biocarrier, strains of P. chrysosporium and P. ostreatus, and filter are useful for the treatment of wastewater contaminated with color, heavy metals and high values of chemical oxygen demand and biochemical oxygen demand (claimed).    ADVANTAGE - The laminar biocarrier can be efficiently used as a filter for reactors of different configurations for the treatment of waste effluents.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a filter for treating wastewater, which comprises: (A) the laminar biocarrier; and (b) a support that allows the adjustment and assembly of laminar biocarrier into the reactor to carry out the treatment; and    (2) a process for preparing the laminar biocarrier, which involves: (a) preparing support consisting of lignocellulosic material taking between 1-10 mm previously washed and dried to form a mesh of any shape, preferably square, with a pore size of 0.1-10 mm; (b) sterilizing the support by applying moist heat and autoclaving for two thermal cycles to 0.72 kPa for a time of 15-90 minutes for every cycle, and cooling the system leaving it closed until being inoculated with the fungal biomass; (c) mixing the biomass from two or more fungal wood rot until a uniform paste consortium biomass; and (d) colonizing support under sterile conditions by adding a layer of between 1-10 mm thick and bran extract agar gel for 10 minutes; placing another lignocellulosic mesh material on the surface of the agar and inoculated meshes sisal uniformly with a layer of biomass in areas equivalent to 0.01-0.5% (mass/volume) and incubating for a time of 5-15 days at a temperature of 25-35 degrees C.
NOVELTY - The method involves characterizing nature of waste (19) introduced into a drum (10). The temperature of waste in the drum is measured. The total mass of waste in drum is determined. The quantity of air and a flow rate of air to be injected are calculated, depending on the measured temperature, determined total mass of the waste, and characterized nature of waste, with reference to a set of data stored in a memory. The calculated quantity of air at calculated flow rate is injected into drum by a fan (17), when inlet shutter (12) and outlet shutter (13) are closed.    USE - Method for regulating ventilation of pre-composting drum for rotary bioreactor used for pre-composting of waste such as household refuse or mud.    ADVANTAGE - The pretreatment of waste can be performed efficiently. The drum is left in rotation and is closed during night time while imprisoning a certain quantity of air, so that air is injected and extracted in a controlled way for improving fermentation of waste in day and the night times and preventing anaerobic mode of drum.    DETAILED DESCRIPTION - An extractor (18) is connected to a network of pipes in which the pressure is equal to a set pressure, for extracting air from the drum. The pressure in the pipe network is measured. The vacuum fan exhaust flow is controlled as a function of the difference between the set pressure and the measured pressure in the pipe network. The amount of air calculated between several fans is divided. An air flow is generated between the fan and the extractor in the direction of scrolling of waste in drum or in the opposite direction of scrolling waste in the drum. An INDEPENDENT CLAIM is included for a computer program for regulating ventilation of pre-composting drum.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of pre-composting drum.    Drum (10)    Inlet shutter (12)    Outlet shutter (13)    Fan (17)    Extractor (18)    Waste (19)
NOVELTY - The apparatus has a target gas adsorption unit that drives a heater layer over target gas adsorption time (t1) at which target gas is adsorbed in an adsorption layer. A target gas desorption unit drives heater layer over target gas desorption time (t2) by target gas desorption temperature (T2) at which target gas absorbed on adsorption layer desorbs, and moves to gas sense layer. A target gas concentration calculation unit computes gas concentration of target gas from the sensor resistance value of gas sense layer after progress of target gas desorption time (t2).    USE - Apparatus for detecting gas such as methane gas, propane gas, commercial butane and carbon monoxide. Can also be used in environmental and medical fields.    ADVANTAGE - The semiconductor type gas sensor is detected by high sensitivity, and the detection concentration range of target gas is expanded to the low concentration side. The density detection sensitivity of VOC is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for detecting gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the timing diagram and graph illustrating the relationship between the temperature of the heater layer, and sensor resistance value. (Drawing includes non-English language text)    Target gas adsorption time (T1)    Target gas desorption temperature (T2)    Target gas detection temperature (T3)    Target gas adsorption time (t1)    Target gas desorption time (t2)
NOVELTY - A visible-light responsive composition comprises 40-90% lead (Pb), 10-40% chromium (Cr), 0-40% iron (Fe), and balance oxygen in which total amount of Pb, Cr, and Fe is made into 100%.    USE - A visible-light responsive composition for photoelectrode and photocatalyst used for hydrolysis method, and photosensor (all claimed).    ADVANTAGE - High photoelectric current responsiveness is demonstrated with respect to visible light irradiation.
NOVELTY - The new type utility claims a biological diesel oil..., wherein a methyl alcohol high-order groove, lipid high-order groove, vitriol high-order groove, a flow meter, a reaction kettle, a glycerin separation tank compose, methanol high-order groove, lipid high-order groove, vitriol high-order groove connected by a flow meter and a reaction pipe, also comprises a reaction kettle, feeding material wherein the second reaction kettle through pipeline connected to glycerin separating tank wherein a glycerol separating tank of biological diesel oil outlet through pipeline connected to a component, a high-order groove comprises a lipid with a one of the following two of round taper hopper, a discharging spiral conveying machine table, the round up with the following two of cone angle of two of the same cone, a cone hopper is provided with leakage holes, conical bucket bottom is provided with a slag hole., a slag hole. the discharging spiral conveying machine.
NOVELTY - The new type utility claims a one for biological diesel production is a extracting device, wherein a pre-filtering module, extracting a pipeline by connecting in turn and a quadratic filter module, a pre-filtering module comprises a lower round the two with a taper hopper, spiral conveying machine, a can with the following two of a cone, a cone hopper is provided with leakage holes, conical bucket bottom is provided with a slag hole., a slag hole. the discharging spiral conveying machine, a part of round tank provided with out oil pipe of the oil out pipe by pipeline for extracting a feeding, the extracting module comprises tank body, a side connected with a reflux pipe and a reflux pipe provided with a reflux pump, a oil inlet provided with a tank body, a steam entrance methyl alcohol and methyl alcohol steam outlet, provided with a control valve on a methanol steam outlet, in the tank body set with multi-layer catalyst layer, on the tank body also has biology diesel oil outlet set, the biological diesel oil outlet through pipeline connected to a quadratic component of feeding wherein.
NOVELTY - The system has the secondary electrolytic cells that are electrically connected to the primary electrolytic cells. The anode terminal and the cathode terminal are electrically connected to the hydrolysis plates. A power source (1) is electrically connected to the control module. The primary electrolytic cells and the secondary electrolytic cells are provided in fluid communication with an air intake duct of a combustion engine through the filtration tank. The generated ortho-Oxyhydrogen improves efficiency of the combustion engine.    USE - Oxyhydrogen gas generating system for vehicle. Uses include but are not limitred to vehicles such as diesel engine automobile, tractor-trailer, motor home, train, ship, combine, barge, cargo-ship, freight-liner, and cruise-liner.    ADVANTAGE - The system generates ortho-Oxyhydrogen gas in order to improve fuel economy and increase horsepower in combustion-powered vehicles. The cylinder head comprises the moisture-collecting chambers while a dehumidifying mechanism is installed within the filtration tank in order to remove moisture from the ortho-Oxyhydrogen gas, such that moisture losses in the electrolytic cells are reduced and the generated gases output to the engine are ensured to be sufficiently dry. The generating system is housed in an enclosed single housing unit for better temperature management and installation or alternatively installed at any desirable and available location on the vehicle so as to place the electrolytic cells adjacent to the engine to make routing the generated gases easier.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the electrical circuit for the electrolytic cells.    Power source (1)    Primary anode generator (61)    First subsidiary anode generator (71)    Second subsidiary anode generator (72)    Second subsidiary cathode generator (74)
NOVELTY - The utility model is new type relates to a biological diesel oil preparing device is a U type tube process strengthening device, fixing a guide rail bracket fixing bolt, sliding plate fixed at the guide rail bracket and a upper bracket left and right move along the guide rail, a sliding plate provided with a bearing base, a base provided with a rotating shaft across shaft base, and bearing by a bearing base fixed on the upper rotating shaft also provided with two of the eccentric rotor, bracket fixed at the guide rail bracket on the U type pipe fixed by a bolt flange fixed reactor, reactor is U type bracket on the left reactor provided with a product outlet, right end provided with the reactant entrance, the inner side reactant entrance also set with entrance valve, a lower reactor of two of the opening provided with a double piston, piston and to; a piston connected at the reactor is also provided with spring screw and a sliding plate, rotating shaft and motor connected. The utility model is new type comprises following beneficial effect: it does not need increase fluid conveying device of energy consumption and a volume that can increase process efficiency.
NOVELTY - The utility model is new type relates to a rotary kitchen waste biochemical processor, a motor and a speed reducer drive bracket support a set of a set of small gear, the small gear and the large gear ring on outside wall outside mesh material, large gear ring storage outside of two side wall set has a roller, a mounting bracket has a roller circumscribing the support roller wheel, front end is set with storage bin has a bin chamber body around the relative rotating axis of rotating joint, a rotating joint has a set of rear end is set with storage bin has a bin chamber around the body axis relative rotating of swing joint, a swing joint has set for gas/water pipe and returning gas/water pipe, air inlet pipe and discharge pipe. The utility model is new type adopt gear transmission rotary cabin structure, thus carrying out stirring for the material in storage hopper, a large amount of driving power needed is small, and the efficiency is high, energy-saving, efficient time when cabin body rotating, rotary joint and swing joint can ensure the normal feeding, discharging, air inlet, and normal discharge of steam/water, returning gas/water, a normal measurement data.
NOVELTY - The molder has an exhaustion die structure that is provided with an eccentric wheel. One exhaustion die (124) is equipped in an external periphery portion of other exhaustion die. A pair of heating element (124b-2) is a heating wire equipped on both sides of a warped surface of a waste material pressed in inside in a longitudinal direction. The first exhaustion die is compressed with the taping force of the eccentric wheel. The exhaustion dies are radially arranged in a turning space outside of the eccentric wheel.    USE - Solid fuel molder.    ADVANTAGE - The structure of the solid fuel molder is improved. The coating performance about the waste flowed in within the outlet molding groove is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a disassembled perspective view of the solid fuel molder.    Exhaustion die (124)    Coating portion (124a)    Heating unit storage unit (124a-1)    Fixing groove (124a-4)    Heating element (124b-2)
NOVELTY - A levodopa is extracted from Stizolobium cochinchinensis seed by pre-processing raw material by removing impurity and crushing to 20-60 meshes, adding with de-ionized water, acetic acid, ascorbic acid and pectinase, mixing uniform, and soaking for 4 hours; performing microwave assistant extraction at 2450 MHz and 20 KW for 45-50 minutes at 55-60 degrees C, and solid-liquid separating; and passing through refined filter ceramic film and ultra-filtration ceramic film.    USE - Method for microwave-assisted extraction of levodopa from S. cochinchinensis seed (claimed).    ADVANTAGE - The method has high efficiency, and does not pollute the environment.    DETAILED DESCRIPTION - Microwave-assisted extraction of levodopa from S. cochinchinensis seed comprises (A) pre-processing raw material by removing impurity and crushing to 20-60 meshes, adding with de-ionized water, acetic acid, ascorbic acid and pectinase, mixing uniform, and soaking for 4 hours; (B) performing microwave assistant extraction at 2450 MHz and 20 KW for 45-50 minutes at 55-60 degrees C, and solid-liquid separating; (C) passing through refined filter ceramic film and ultra-filtration ceramic film; (D) taking filtered liquid, reverse permeability film filtering, and concentrating; (E) taking concentrated filtered liquid and evaporation concentrating to obtain paste-shaped object; (F) crystallizing by adding the paste-shaped object in acid dissolution tank with hydrochloric acid solution, dissolving, filtering, neutralizing, taking into crystallizing tank, and adjusting pH value to 4. 5; (G) separating using centrifuge; (H) taking filtered liquid for further concentrating, crystallizing, washing and drying, and solid-liquid separating; and (I) washing with deionized water and then with anhydrous ethyl alcohol, and vacuum drying.
NOVELTY - An electrolyte comprises a nonaqueous solvent, lithium salt and a deuterium-substituted compound (I) or (II).    USE - Electrolyte is used for lithium secondary battery (claimed).    DETAILED DESCRIPTION - An electrolyte comprises a nonaqueous solvent, lithium salt and a deuterium-substituted compound of formula (I) or (II).    R1-R7,R11-R13=H, deuterium or 1-9C alkyl substituted with deuterium, in which at least one of R1-R7 and R11-R13 is D;and    A=1-9C alkyl.    An INDEPENDENT CLAIM is included for lithium secondary battery.
NOVELTY - Producing solid protein feed product from wastewater, involves (a) growing microbial cells in aqueous waste stream to produce waste activated sludge, (b) drying the dewatered waste activated sludge to solids content of 80-90 wt.% solids, and (c) sterilizing the waste activated sludge before, during or after the dewatering or the drying to provide solid protein feed product which is commercially sterile, where protein quality of the solid protein feed product is substantially unchanged from that of the waste activated sludge before sterilizing and drying steps.    USE - The method is useful for producing solid protein feed product from wastewater, where the solid protein feed product is used in agricultural fertilizer (all claimed). The solid protein feed product is animal feed or human food product.    ADVANTAGE - The method has improved microbial protein quality, storage stability and/or process economics, and lower live bacterial load.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid protein feed product which is prepared by the above-mentioned method.
NOVELTY - A plant system comprises a blast furnace for iron-making, a converter steelwork for production of crude steel, and a gas pipeline system for collecting and supplying gases obtained during the production of pig iron and/or steel. The gas pipeline system is connected to a chemical plant or biotechnology plant and a system for hydrogen production, which is connected to gas conduit system.    USE - Plant system is used for steelmaking.    ADVANTAGE - The plant system can be operated economically.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of operating plant system; and    (2) usage method of chemical or biotechnology plant in conjunction with hydrogen production system.
NOVELTY - The device has an electrolysis cell for chlorine-alkali electrolysis, having an anode half-cell (1), a cathode half-cell (2) and a cation-exchange membrane (3). An anode (4) is arranged in anode half-cell for development of chlorine. An oxygen-consuming electrode (5) is arranged in cathode half-cell as cathode. A gas space (7) is formed adjoining the electrode on surface facing away from a catholyte (6). A second cathode (9) is arranged in the catholyte for generating hydrogen, and a line (10) for flushing the gas space with inert gas is formed.    USE - Device for flexible use of electricity, for producing hydrogen from excess electrical energy.    ADVANTAGE - Flexible use of electricity is made possible in a process in which gaseous oxygen is fed to oxygen-consuming electrode when there is low supply of electricity. The device has low expenditure, and the proportion of electrolysis cells in which hydrogen is produced is varied. The chlorine amount used when rinsing is reduced. High purity and consistent quality of hydrogen is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for flexible use of electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for flexible use of electricity.    Anode half-cell (1)    Cathode half-cell (2)    Cation-exchange membrane (3)    Anode (4)    Oxygen-consuming electrode (5)    Catholyte (6)    Gas space (7)    Second cathode (9)    Line for flushing the gas space (10)
NOVELTY - A biodiversity garden constructing method involves utilizing three-dimensional ecological community planting mode comprising water white shading as upper layer, ecological tea plants as lower layer and weed and green manure crops as bottom layer.    USE - Method for constructing biodiversity garden.    ADVANTAGE - The method enables constructing biodiversity garden with increased soil fertility, yield and quality of plants.
NOVELTY - A sensing material comprises nickel vanadium oxide nanofibers.    USE - Sensing material for a gas sensor (claimed) that is utilized in field of health care, surveillance of environmental pollution, industrial safety, home appliances, food and agricultural field, and national defense and prevention of terrorism.    ADVANTAGE - The material is prepared in a simple, easy and economical manner, provides high quality of the gas sensor, and has improved sensitivity to a target gas.    DETAILED DESCRIPTION - A sensing material comprises nickel vanadium oxide (Ni3V2O8) nanofibers. INDEPENDENT CLAIMS are also included for the following:    (1) a gas sensor    (2) a method for preparing a sensing material.
NOVELTY - Preparation of catalyst comprises washing ostrich eggshell with distilled water, removing impurities, and drying at 90-110 degrees C for 12-20 hours; crushing and sieving through 160-180 meshes sieve; placing into muffle furnace, calcining at 800-1000 degrees C under nitrogen conditions, and vacuum drying.    USE - Method for preparing catalyst used for preparing biodiesel (claimed).    ADVANTAGE - The method has low cost, wide raw material source, biodiesel production rate of more than 90%, and biodiesel yield of more than 80%. The catalyst has regeneration effect and strong catalytic activity and can be recovered for 6 times.
NOVELTY - Denatured alcohol comprises 90-95 pts. wt. phase material A and 5-10 pts. wt. phase material B, where the phase material A comprises alcohol and light oil. The phase material B comprises methane and dimethyl ether.    USE - Denatured alcohol used as fuel for vehicle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing denatured alcohol, which involves using alcohol, light oil, methane and dimethyl ether.
NOVELTY - Hydrogen gas manufacturing device (100) comprises an anode plate (110), a cathode plate (120) and an electric conduction plate (130), which is provided between the anode plate and the cathode plate. Insulation sealing element (140) is provided between the anode plate and the electric conduction plate. The cathode plate, electric conduction plate and adjacent electric conduction plate are surrounded by insulation sealing element. The anode plate, cathode plate and the electric conduction plate are provided with a hole.    USE - Hydrogen gas manufacturing device.    ADVANTAGE - The hydrogen gas manufacturing device reduces discharge of carbon monoxide and nitrogen monoxide, and thus protects environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen gas manufacturing device.    Hydrogen gas manufacturing device (100)    Anode plate (110)    Cathode plate (120)    Electric conduction plate (130)    Insulation sealing element (140)
NOVELTY - Preparing composite photoelectric cathode involves putting indium tin oxide glass substrate in nickel(II) nitrate solution and hexamethylenetetramine and then heating at 100 degrees C for 12 minutes to obtain nickel-indium tin oxide glass substrate. The nickel-indium tin oxide glass substrate is washed with deionized water and then dried at 300 degrees C. The nickel-indium tin oxide glass substrate is heated for 30 minutes and then put into cadmium and selenium dissolved in ethanol to obtain nickel-cadmium selenide-indium tin oxide glass substrate.    USE - Method for preparing composite photoelectric cathode used for photovoltaic catalytic water decomposing for production of hydrogen.    ADVANTAGE - The method enables to prepare composite photoelectric cathode, that has high catalytic activity and stable performance.    DETAILED DESCRIPTION - Preparing composite photoelectric cathode involves putting indium tin oxide glass substrate in nickel(II) nitrate solution and hexamethylenetetramine and then heating at 100 degrees C for 12 minutes to obtain nickel-indium tin oxide glass substrate. The nickel-indium tin oxide glass substrate is washed with deionized water and then dried at 300 degrees C. The nickel-indium tin oxide glass substrate is heated for 30 minutes and then put into cadmium and selenium dissolved in ethanol to obtain nickel-cadmium selenide-indium tin oxide glass substrate. Molybdenum disulfide is deposited on nickel-cadmium selenide-indium tin oxide glass substrate using ammonium tetrathiomolybdate solution to obtain the product.
NOVELTY - Ester of saturated carboxylic acid is synthesized by subjecting polyhydroxycarboxylic acid to deoxydehydration catalyst to remove hydroxyl groups and performing hydrogen transfer reaction.    USE - Synthesis of ester of saturated carboxylic acid used in biofuels for generating biorenewable materials.    ADVANTAGE - The method is sustainable and environment-friendly, achieves quantitative yield of almost 99% compared to the 60% yield of conventional processes, and has mild reaction conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) ester of adipic acid which is synthesized according to the method;    (2) synthesis of ester of adipic acid which involves subjecting mucic acid to deoxydehydration catalyst in the presence of hydrogen transfer catalyst;    (3) synthesis of ester of adipic acid which involves subjecting mucic acid to dehydration catalyst to form ester of muconic acid and performing hydrogen transfer reaction on ester of muconic acid; and    (4) synthesis of saturated carboxylic acid which involves subjecting polyhydroxycarboxylic acid to deoxydehydration catalyst to remove hydroxyl groups, performing hydrogen transfer reaction to form ester of saturated polycarboxylic acid, and hydrolyzing ester.    DESCRIPTION OF DRAWING(S) - The drawing shows a reaction scheme of the conversion of mucic acid to muconic acid and adipic acid.
NOVELTY - The manufacturing method involves applying the silicone coating liquid used as the silicone resin layer to the surface of the porous support with the roll-to-roll system. The viscosity of the silicone coating liquid in shall be 300 centipoise or more when a largest hole diameter coats to the surface of the porous support further, as porous support using the porous body is 5 micrometers or less.    USE - Manufacturing method for composite body utilized for acidic gas separation membrane used for manufacture of hydrogen gas or refinement of natural gas.    ADVANTAGE - The silicone resin layer prevents that a facilitated-transport film is entrapped into porous support, thus, the permeation of the facilitated-transport film to porous support can be prevented, and the acidic gas separation membrane having excellent durability can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the manufacturing apparatus which enforces the manufacturing method of the composite body.    Elongate porous support (12)    Manufacturing apparatus (20)    Supply unit (24)    Coiling (30)    Backup roller (34)
NOVELTY - A fuel gas is desulfurized by being circulated to a desulfurizer comprising a hydrodesulfurization catalyst precursor nickel ion. The fuel gas with sulfur content is circulated with hydrogen in the desulfurizer, and the precursor is reduced to obtain a hydrodesulfurization catalyst.    USE - Desulfurization of fuel gas used in hydrogen-production system of fuel-cell systems (all claimed).    ADVANTAGE - The method enables economical desulfurization of fuel gas without requiring preprocessing and re-reduction processing.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of desulfurization catalyst;    (2) desulfurization system (20) consisting of a desulfurization unit (3) for removing sulfur content from fuel gas, and a fuel supply unit (2) for supplying fuel to the desulfurization unit; and    (3) hydrogen production system (30) provided with a hydrogen-production unit (4) which generates hydrogen from the desulfurized fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual view of a fuel-cell system. (Drawing includes non-English language text)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-production unit (4)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - Method (M1) for producing compost, involves subjecting plant-derived organic waste to a fermentation treatment using microorganism of Bacillus subtilis strain C-3102 (FERM BP-1096) or its mutant strain, and composting the organic waste at a weight reduction rate of 95% or more, where the fermentation treatment comprises primary fermentation, which comprises an intermittently agitated fermentation, and a secondary fermentation, which comprises an aerated fermentation.    USE - The method is useful for producing compost which is used for producing vegetables. The vegetable is a root vegetable. The vegetable is Japanese white radish or carrot (all claimed). The compost is also used for producing flowers, and ornamental plants.    ADVANTAGE - The method enables to produce compost with good quality. The produced compost enables to produce vegetables with improved taste, bitterness, astringency and saltiness, and increased yield as compared to a control compost produced from organic waste in absence of microorganism.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M2) for producing a vegetable involves cultivating a vegetable using a compost obtained by subjecting plant-derived organic waste to a fermentation treatment with B.subtilis strain C-3102 (FERM BP-1096) or its mutant strain to produce vegetable with an improved taste compared to a control compost produced from organic waste in absence of the microorganism; and (2) method (M3) for increasing amount of vegetable production involves cultivating a vegetable using a compost obtained by subjecting plant-derived organic waste to a fermentation treatment with a microorganism of B.subtilis strain C-3102 (FERM BP-1096) or its mutant strain, and increasing amount of produced vegetable compared to a control compost produced from the organic waste in the absence of the microorganism.
NOVELTY - This utility new type claims a. processing of waste water microorganism deodorizing device. D, large and small water tank composed of the large front water tank provided with a water inlet, small water tank set with end. wherein water, large water pool and a separate wall between a separate wall and is a small pool between part provided with a through hole, the utility model is new type of a feature is, for water provided with filter screen, wherein a part of water close to the water inlet is provided with a microorganism deodorant feeding tank, a small water close to the water outlet of the upper part provided with a water pump. After processing of waste water through a network entering into a large water tank, a microorganism deodorant in tank body is periodically added with large water pool, a water pump, a small water tank water body rich in beneficial microorganism is continuously pump of the large water tank water inlet, a finish of processing waste water from a fast up source, lasting. This utility new type also comprises preparation and use is simple, the cost is low.
NOVELTY - A biomass solid fuel is obtained by kneading bamboo charcoal powder with sewage sludge and solidifying, and has heat amount of 4000 Kcal or more and ash content of less than 30 vol.% after combustion.    USE - Biomass solid fuel (claimed).    ADVANTAGE - The biomass solid fuel having high heat amount during combustion and reduced ash content after combustion is manufactured. The tar contained in the bamboo acid liquid acts as a thickener and prevents the shape loss of the biomass sold fuel. The bamboo charcoal powder is very fine and porous, and has excellent deodorization and antimicrobial effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the biomass solid fuel, which involves kneading 5-30 wt.% bamboo charcoal with refinement degree of 3 or less obtained by self sustained-combustion-carbonization-type reduction method with 70-95 wt.% sewage sludge, and solidifying to moisture content of 10 wt.% or less.
NOVELTY - Manufacture of fat and oil-containing triterpene alcohol involves carrying out alkaline hydrolysis of ( gamma )-oryzanol-containing raw material, neutralizing hydrolyzate using acid such that neutralization degree reaches 0.9-1.05 with respect to amount of residual alkali, mixing the neutralized material with fats and oils, and obtaining fat and oil-containing triterpene alcohol.    USE - Manufacture of fat and oil-containing triterpene alcohol used for lowering blood cholesterol.    ADVANTAGE - The method enables manufacture of fat and oil-containing triterpene alcohol with excellent external appearance at normal temperature, and low-temperature tolerance, and high purity and triterpene alcohol concentration, by environmentally-friendly process.
NOVELTY - The gas concentration measurement device (Z1) comprises an air supply path (1) that is provided with an inlet port, which inhales to-be-test gas, and with an exhaust port, which discharges the to-be-test gas after completion of inspection. An air-supplying apparatus (4) is provided with an ejector, which supplies the to-be-test gas by introducing compressed air or compressed nitrogen in the air supply path.    USE - Gas concentration measurement device for measuring concentration of detection target gas contained in to-be-test gas.    ADVANTAGE - The gas concentration measurement device comprises an air supply path that is provided with an inlet port, which inhales to-be-test gas, and with an exhaust port, which discharges the to-be-test gas after completion of inspection, and thus performs the concentration measurement of detection target gas safely with high precision.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method measuring concentration of the detection target gas contained in the to-be-test gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a gas concentration measurement device.    Air supply path (1)    Air-supplying apparatus (4)    Accumulator (6)    Ventilation path (10)    Gas concentration measurement device (Z1)
NOVELTY - This utility new type relates to a a a a livestock and poultry excrement of type composting device belongs to environment-friendly device technology field. A columnar box body, multi-layer turning system, multi-layer gas distribution pipe and hopper, multi-layer turning system and corresponding multi-layer gas distribution tube transverse uniformity of the inner cylindrical body, pipe through air inlet pipe and the fan connected, over a reverse turning bed is fixed a reverse turning bed shaft on the turning operation stick and reverse turning bed interaction shaft is columnar tank body outside wall over, reverse turning bed shaft double end fixed on a wall inner columnar box body, reverse turning bed shaft through reverse turning bed interaction stick and reverse turning bed shaft interaction interaction, a reverse turning bed. The composting device using aerobic fermentation, running period short, processing efficiency is high, each layer box body is columnar is a fermentation chamber, a transfer and a rotating turning finish waste on reverse turning bed is, simple operation, low energy consumption, and small square meter is small, convenient to maintain, a reverse turning bed set with vent hole, increase the air capacity, reducing the fan energy consumption, and make distribution more uniform.
NOVELTY - The power generation plant has a component wood gas generator (2) that is connected with a downstream filter (3) that is connected with a wood gas cooler (4). A wood gas tank (7) is connected with an upstream compressor (6) that is connected with a wood gas dispensing system (10). The heat exchangers are provided in the wood gas generator and on wood gas cooler and a controller (11) is connected to all components in the plant. The wood gas dispensing system is connected with a cogeneration unit (9).    USE - Stationary power generation plant for use in home, for producing heat, electricity and wood gas for use as fuel for gas-powered motor car.    ADVANTAGE - The efficiency of the power generation plant is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the power generation plant.    Wood gas generator (2)    Downstream filter (3)    Wood gas cooler (4)    Upstream compressor (6)    Wood gas tank (7)    Cogeneration unit (9)    Wood gas dispensing system (10)    Controller (11)
NOVELTY - Delayed coking process involves subjecting a mixed feed comprising residual heavy hydrocarbon feedstock and bio oil obtained from fast pyrolysis of lignocellulosic biomass (1) of Jatropha, cashew nut, karanja and neem to delayed coking process.    USE - Delayed coking process (claimed).    ADVANTAGE - The delayed coking process of mixed feed is performed to improve gas and liquid yields, and reduce coke yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for delayed coking process, which includes an online or offline mixing mechanism for mixing residual heavy hydrocarbon feedstock (9) and bio oil, and a coking drum (18) for delayed coking of the mixed feed.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating delayed coking process.    Lignocellulosic biomass (1)    Bio oil recovery unit (7)    Residual heavy hydrocarbon feedstock (9)    Fractionator (11)    Coking drum (18)
NOVELTY - A triacylglycerides-containing oils or fatty acids converting method involves feeding hydrogen, water and triacylglyceride-containing oil into a co-current reactor having a homogeneously catalyzed hydrothermolysis reaction zone and a heterogeneously catalyzed hydrotreatment zone, and hydrothermolyzing a portion of the triacylglyceride-containing oil in the hydrothermolysis reaction zone to form a hydrothermolysis reaction product, which is hydrotreated directly without componential separations in the hydrotreatment zone, followed by recovering an effluent from the hydrotreatment zone.    USE - Method for converting triacylglycerides-containing oils or fatty acids derived from plants, algae, organic wastes or animal sources into crude oil precursors and/or distillate hydrocarbon fuels.    ADVANTAGE - The method enables converting triacylglycerides-containing oils or fatty acids into crude oil precursors and/or distillate hydrocarbon fuels with high density, high energy density, good low-temperature properties (freezing point, cloud point, pour point, and viscosity), natural lubricity, wide range of hydrocarbon types and molecular weights similar to petroleum distillates and/or good thermal stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for converting triacylglycerides-containing oils or fatty acids derived from plants, algae, organic wastes or animal sources into crude oil precursors and/or distillate hydrocarbon fuels.
NOVELTY - Method for performing enhanced fermentation through genetic modification of yeast, involves (a) stably integrating inducible promoter coding sequence operably linked to mitochondrial targeting signal coding sequence into yeast, where the mitochondrial targeting signal coding sequence is operably linked to at least one restriction enzyme coding sequence, (b) inducing expression of at least one restriction enzyme, where at least one restriction enzyme targets and destroys the mitochondrial DNA of the yeast, and (c) inducing enhanced fermentation by the yeast.    USE - The method is useful for performing enhanced fermentation through genetic modification of yeast which is useful in biofuel production.    ADVANTAGE - The method stably integrates DNA construct in the yeast.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) DNA construct for enhanced yeast fermentation through genetic modification of yeast comprising inducible promoter, at least one restriction enzyme operably linked to the inducible promoter, and mitochondrial targeting signal coding sequence; and    (2) transgenic yeast having stably integrated DNA construct in a suitable conditions for expression of the above-mentioned DNA construct, where the DNA construct expresses restriction enzyme targeted at the mitochondrial DNA of the transgenic yeast.
NOVELTY - A sludge-disposal apparatus (1) comprises substrate tank (2) which stores and supplies culture medium, biocatalyst culture tank (3) which cultures biocatalyst, and digester (4) which anaerobically digests organic sludge and converts into biogas.    USE - A sludge-disposal apparatus.    ADVANTAGE - The apparatus can efficiently improve gas conversion rate of organic sludge and shorten digestive residence time without injecting large-scale incidental equipment and energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge-disposal method which involves supplying culture medium to biocatalyst, culturing biocatalyst, solubilizing organic sludge using the biocatalyst, and carrying out anaerobic digestion treatment of organic sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the sludge-disposal apparatus. (Drawing includes non-English language text).    Sludge-disposal apparatus (1)    Substrate tank (2)    Biocatalyst culture tank (3)    Digester (4)    Dehydrator (5)
NOVELTY - Biomass treatment system comprises a processing unit and a production unit, where processing unit comprises a straw crushing device (1), a straw burdening mixing device (2), a conveying device (3), a measuring device (4) and a multiflash explosion straw device (5). The production unit comprises biomass straw feed production line (6), edible powder production line, pulping production line, biological alcohol fuel production line and wood-plastic composite building material production line and pulping biological alcohol fuel production line.    USE - Biomass treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass treatment system.    Straw crushing device (1)    Straw burdening mixing device (2)    Conveying device (3)    Measuring device (4)    Multiflash explosion straw device (5)    Biomass straw feed production line (6)
NOVELTY - Insect repellent incense ball comprises 35-40 pts. wt. Litsea cubeba powder, 8-10 pts. wt. Cedrela sinensis leaves powder, 20-25 pts. wt. Chinese prickly ash powder, 18-25 pts. wt. peony skin powder, 20-25 pts. wt. lavender powder, 10-15 pts. wt. mint powder, 20-25 pts. wt. 80 meshes talc, 2-5 pts. wt. Sesbania powder, and 35-40 pts. wt. water.    USE - Insect repellent incense ball used for cabinet (claimed).    ADVANTAGE - The low-cost and convenient to use ball is mothproof, has little toxicity, and safe and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of insect repellent incense ball comprising collecting green belt stem spinnate, cooling and ventilating until moisture content of 15-20%, preparing ozone Cedrela sinensis leaves; taking bark of tree peony root, peppermint, pepper and lavender, drying and deodorizing Cedrela sinensis leaves and Litsea cubeba, drying until moisture content of 10-13%, grinding, passing through 60 meshes screen network to prepare tree peony powder, mint powder, pepper powder, lavender powder, Cedrela sinensis leaves powder and Litsea cubeba powder; taking rhizoma atractylodis, Cedrela sinensis leaves powder, Chinese prickly ash powder, peony skin powder, lavender powder, mint powder, talc, and Sesbania powder; stirring, gradually adding clean water, stirring for 7-8 minutes; and manufacturing incense ball with diameter of 1-1.2 cm, and drying to water content of 6-10%.
NOVELTY - Fenbendazole microsphere is prepared by forming gelatin solution using gelatin and water, heating to 45-55 degrees C, adding fenbendazole to obtain water phase containing 0.02-0.4 g/ml gelatin and 0.01-0.5 g/ml fenbendazole, mixing liquid paraffin:1-2 mass% Span 80 (RTM: Nonionic surfactant) with volume ratio of 4-6:1 to obtain oil phase, mixing water phase:oil phase with volume ratio of 1:5-7, cooling to less than or equal to 5 degrees C, adding glutaraldehyde with volume ratio glutaraldehyde:water phase of 1:1-10, crosslinking, washing with isopropanol, washing with petroleum ether, and vacuum-drying.    USE - Preparation of fenbendazole microsphere.    ADVANTAGE - Fenbendazole microsphere has prolonged drug elimination half life and improved encapsulation efficiency, and preparation is simple, safe, environment-friendly, and low-cost.
NOVELTY - A biodiesel and glycerin continuous separation device comprises feed pump connected to rectifier via conduit; tank body connected to glycerin tank, swash plate coalescer, regulating weir plate and overflow pipe connected to biological diesel oil tank; tank cover provided with gas outlet connected to condensing pipe via conduit; methanol storage tank provided with feed port; discharge pump; inner warming jacket; outer insulating layer.    USE - Biodiesel and glycerin continuous separation device.
NOVELTY - Engine fuel reformation involves atomizing engine fuel into plasma generator through an atomizer. A high voltage is applied to electrodes including center electrode (1) and outer electrode (3) in high-voltage action. The center electrode and the outer electrode promote high-speed rotation of the vegetable oil by using the narrowest point arc plasma generator. The obtained non-thermal arc plasma is reformed to produce a hydrogen-rich gas mixture.    USE - Method for reforming engine fuel for producing hydrogen (claimed).    ADVANTAGE - The method produces hydrogen gas in a simple and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the vegetable oil reformation method.    Center electrode (1)    Polytetrafluoroethylene layer (2)    Outer electrode (3)    Cylindrical outer wall (4)    Outlet (6)
NOVELTY - Organic fertilizer comprises 90-110 pts. wt. sewage sludge, 1.5-2.5 pts. wt. dispersing agent, 0.05-0.15 pts. wt. leavening agent and 0.4-0.6 pts. wt. quicklime.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer ensures harmless recycling of sludge and thus prevents pollution caused by sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing and drying sewage sludge and dispersing agent;    (B) fermenting obtained mixture with leavening agent in fermentation tank aerobically for 10-15 days;    (C) fermenting fermented materials with quicklime in anaerobic medium covered with rubber thin film for 8-12 days;    (D) drying, crushing and granulating fermented materials; and    (E) cooling and sieving to obtain granules to obtain product.
NOVELTY - A methane is separated from concentrated coke oven gas by pressurizing coke oven gas into aqueous tetrahydrofuran solution, reacting, cooling, generating solid-aquo complex, heating, and decomposing.    USE - Methane separation method from concentrated coke oven gas (claimed).    ADVANTAGE - The method is simple and low-cost.
NOVELTY - The device has a pyrolysis reactor (5) whose inlet end is connected with an outlet end of a loading pneumatic (15). The pyrolysis reactor is connected with a pneumatic cyclone separator (6). The outlet end of the loading pneumatic is connected with a rotary dust remover (7). A product storage tank (13) is connected with an outlet end of a liquid fuel. A front end of an integrated electronic controller (14) is connected with a swash-plate collector (1), a pulverizer (2), the pyrolysis reactor, the rotary dust remover, a condenser (8), and a tail pneumatic processing device (12).    USE - Movable straw pyrolysis liquid fuel preparation device.    ADVANTAGE - The device ensures low cost biomass fuel preparation and obtains high quality biological oil in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a movable straw pyrolysis liquid fuel preparation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a movable straw pyrolysis liquid fuel preparation device.'(Drawing includes non-English language text)'    Swash-plate collector (1)    Pulverizer (2)    Pyrolysis reactor (5)    Pneumatic cyclone separator (6)    Rotary dust remover (7)    Condenser (8)    Tail pneumatic processing device (12)    Product storage tank (13)    Integrated electronic controller (14)    Loading pneumatic (15)
NOVELTY - The furnace has a gasification furnace body whose upper part is provided with a rubbish gasification room (1) and a water vapor room (2). An inner side of the gasification furnace body is made of refractory material. Lower parts of the rubbish gasification room and water vapor room are connected between water cold furnace arches (3). The water vapor room is arranged with two plasma torches (8), which are provided with an alpha angle. The angle alpha is 120 degrees to 150 degrees. Temperature of the plasma torch and water vapor room is between 150 and 250 degrees Celsius.    USE - Waste plasma gasification furnace.    ADVANTAGE - The furnace provides high-temperature gasification reaction, high-energy environment and material heating rate, and has high effective reaction rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a waste plasma gasification furnace.'(Drawing includes non-English language text)'    Rubbish gasification room (1)    Water vapor room (2)    Water cold furnace arch (3)    Feeding port (4)    Plasma torches (8)
NOVELTY - Alcohol-based fuel comprises 9.6-25.6 pts. wt. 4-ethoxy benzophenone, 11.8-30.3 pts. wt. 2-hydroxy-3-methyl-pentanoate, 12.9-28.1 pts. wt. 1-eth-1-ynyl-4-(pentyloxy)benzene, 14.8-33.5 pts. wt. 2-(4-methoxy-1,4-cyclohexadien-1-yl)-2-propanol, 11.9-27.8 pts. wt. 3-methyl-1-indanone and 10.4-21.6 pts. wt. 1-isopropenyl-4-methoxybenzene.    USE - Alcohol-based fuel.    ADVANTAGE - The alcohol-based fuel suppresses emission of nitrogen oxide.
NOVELTY - Concentrating and separating methane gas involves compressing low-concentration methane gas successively and then purifying the compressed material. The purified material is deoxygenated by pressure swing adsorption process and then the deoxygenated material is subjected for second level pressure swing adsorption for removing nitrogen. The obtained material is subjected to a third level transformation process for concentrating and separating explosion limit of methane gas.    USE - Method for concentrating and separating methane gas (claimed).    ADVANTAGE - The method enables to concentrate and separate methane gas with high concentration and separation efficiency, and has improved concentration of methane gas from 5-20% to 80-90%.
NOVELTY - Preparing biodiesel involves carrying out transesterification of lipid with guanidinylated bioreducible polymer in presence of alcohol, alkali and catalyst.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method is easy to implement continuous production of biodiesel through catalytic transesterification in a cost-effective manner..
NOVELTY - Hydrogen generation system comprises electrolytic machine, heat exchanger (14) and current power supply. The heat exchanger is provided with aluminum radiating fin, where aluminum radiating fin is microchannel heat exchanger. The heat exchanger is installed with an upper collecting pipe (6), lower collecting pipe and a terminal pneuma (13). The terminal pneuma is provided with hydrogen outlet pipe (7). The middle flat pipe is provided with spray water device. The spray water device comprises spray pipe and a spray tube. The spray tube is connected with a fixed block (10).    USE - Hydrogen generation system.    DETAILED DESCRIPTION - Hydrogen generation system comprises electrolytic machine, heat exchanger and current power supply. The heat exchanger is provided with aluminum radiating fin, where aluminum radiating fin is microchannel heat exchanger. The heat exchanger is installed with an upper collecting pipe, lower collecting pipe and a terminal pneuma. The terminal pneuma is provided with hydrogen outlet pipe. The middle flat pipe is provided with spray water device. The spray water device comprises spray pipe and a spray tube. The spray tube is connected with a fixed block. The inner wall of the box body is provided with air cylinder and telescopic column.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen generation system.    Upper collecting pipe (6)    Hydrogen outlet pipe (7)    Fixed block (10)    Terminal pneuma (13)    Heat exchanger (14)
NOVELTY - Extraction of lipids and sugars from algal biomass, comprises: producing an aqueous suspension of algal biomass; bringing the pH of the algal biomass to a value greater than or equal to 10, preferably 10.2-12; adding at least one anionic flocculant to the aqueous suspension of algal biomass at basic pH; subjecting the concentrated algal biomass to lipid extraction to obtain an organic phase comprising lipids and a semi-solid phase comprising a residue of the algal biomass; and subjecting the semi-solid phase to hydrolysis to obtain sugars.    USE - The process is useful for the extraction of lipids and sugars from algal biomass, where the lipids are useful in the production of biodiesel or green diesel which can be used as such, or in a mixture with other fuels for motor vehicles, the sugars are used as carbon sources in fermentation processes for the production of lipids and also for the production of alcohols (e.g. ethanol and butanol), and the alcohols are used as biofuels for motor vehicles or as components that can be added to fuels for motor vehicles.    ADVANTAGE - The process is reproducible and can be applied on an industrial scale.    DETAILED DESCRIPTION - Extraction of lipids and sugars from algal biomass, comprises: producing an aqueous suspension of algal biomass; bringing the pH of the algal biomass to a value greater than or equal to 10, preferably 10.2-12, to obtain an aqueous suspension of algal biomass at basic pH; adding at least one anionic flocculant to the aqueous suspension of algal biomass at basic pH to obtain a concentrated algal biomass; recovering the concentrated algal biomass; subjecting the concentrated algal biomass to lipid extraction to obtain an organic phase comprising lipids and a semi-solid phase comprising a residue of the algal biomass; and subjecting the semi-solid phase to hydrolysis to obtain sugars.
NOVELTY - A fuel reforming system comprises modifier (15) containing a modification catalyst (152), a mixer (14) which is provided upstream of the modifier, and a condenser (16) which is provided downstream of the modifier and separates the gas produced in modifier into gas phase and condensed phase in which the modified fuel is primary constituent. The modification catalyst includes a main catalyst for extracting hydrogen atoms from hydrocarbon in gasoline to produce alkyl radicals, and a catalytic promoter for reducing alkyl hydroperoxides produced from alkyl radicals to produce alcohol.    USE - Fuel reforming system is used for converting fuel into alcohol in vehicle.    ADVANTAGE - The fuel reforming system improves the octane number of the fuel by modifying the fuel containing hydrocarbon.    DETAILED DESCRIPTION - A fuel reforming system comprises modifier containing a modification catalyst which modifies the fuel mainly having a hydrocarbon using air, and produces alcohol, a mixer which is provided upstream of the modifier, and mixes the fuel and air, and supplies the mixture to the modifier, and a condenser which is provided downstream of the modifier and separates the gas produced in modifier into gas phase and condensed phase in which the modified fuel is primary constituent. The modification catalyst includes a main catalyst for extracting hydrogen atoms from hydrocarbon in gasoline to produce alkyl radicals, and a catalytic promoter for reducing alkyl hydroperoxides produced from alkyl radicals to produce alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel reforming system. (Drawing includes non-English language text)    Fuel reforming system (1)    Fuel tank (12)    Mixer (14)    Modifier (15)    Condenser (16)    Fuel supply unit (17)    Reformed fuel tank (18)    Reformed fuel supply unit (19)    Gaseous-phase supply unit (20)    Modification catalyst (152)
NOVELTY - A skid-mounted a microorganism desulphurization and sulphur recovery device, comprising absorption tower, bioreactor, sedimentation groove, pregnant solution groove, poor liquid groove, a clean water tank, a centrifuge, a sulphur recovery groove, poor liquid pump, solution pump equal device. The tower top and lean liquid groove and water cleaning groove by barren liquid pump and pipeline connected, pregnant solution groove and the bottom of the bioreactor by pregnant solution pump and pipe connected the bioreactor and the sedimentation groove through pipeline connected, sedimentation groove top part and lean liquid groove through pipeline connected, sedimentation groove bottom and centrifuge through pipeline connected, centrifuge and sulphur recovery groove and bioreactor through pipeline connected. This device comprises simple structure, convenient operation, stable operation safety and automatic degree high desulphurization efficiency is high and equal.
NOVELTY - An engineered microbial strain capable of converting methane to biofuel and reversing methylreductase to capture methane, is new.    USE - The engineered microbial strain is useful for producing biofuel, preferably ethanol or butanol (all claimed).    ADVANTAGE - The strain converts methane reserves into liquid fuels, reduces greenhouse gas from atmosphere, and provides conversion of methane gas into liquid fuels in easy, reliable and efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system having first engineered organism which comprises methlyreductase capable of capturing methane to produce an intermediate, and second engineered organism that converts the intermediate into biofuel; and    (2) method for producing biofuel, involves providing modified first organism.
NOVELTY - A bio oil-derived residue composition has an initial boiling point of at least 650 degrees F, and comprises 70 wt.% or more aromatic hydrocarbon comprising polycyclic aromatic compound having 4 or more rings. The content of polycyclic aromatic compound contained in the bio oil-derived residue composition is less than 3 wt.%.    USE - Bio oil-derived residue composition is used for tire compound (claimed).    ADVANTAGE - The noncarcinogenic bio oil-derived residue composition has excellent solvency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of bio oil-derived residue composition, which involves converting biomass in a conversion reactor containing a heat transfer medium to produce a conversion reactor effluent comprising vapor conversion product, condensing at least a portion of the vapor conversion product to produce a condensate comprising bio oil and water, where the bio-oil has a total organic oxygen content of less than 40 wt.%, hydrotreating the bio-oil with hydrogen in a hydrotreater reactor to produce a hydrotreater reactor effluent, separating a total liquid product from the hydrotreater reactor effluent, and separating the bio oil-derived residue composition from the total liquid product; and    (2) tire compound, which comprises the bio oil-derived residue, polymer and filler.
NOVELTY - A green alga variant with suppressed dual-specificity tyrosine-regulated kinase (DYRK) activity, is new. The green alga variant comprises DYRK having active site and substrate recognition site, and which comprises an amino acid sequence exhibiting at least 50% sequence identity with respect to a 83 amino acid sequence (SEQ ID NO: 4) fully defined in the specification. The green alga variant provides improved lipid throughput per unit cultivation area and unit time when compared to parent strain.    USE - The green alga variant is useful for producing lipid (claimed) and biofuel.    ADVANTAGE - The green alga variant provides improved lipid throughput per unit cultivation area and unit time when compared to parent strain, and reduces production cost of lipid.
NOVELTY - An organic waste (Y) is processed by heating carbonization container (11) which is inside combustion furnace and contains waste oil (Z) and/or paraffin with boiling point of greater than or equal to 270 degrees C and organic waste with boiling point of greater than or equal to 300 degrees C by carbonization furnace (1) at greater than or equal to 300 degrees C in which gas discharged from gas emission part (11c) and collected at upper part of carbonization container is burned by combustion furnace, and carbonization is completed when waste oil and/or paraffin are evaporated.    USE - Processing of organic waste, such as organic-substance-containing waste material, animal excrement, and wood-bamboo material (all claimed).    ADVANTAGE - Temperature in container can be heated uniformly, and organic waste can be carbonized efficiently for use as heat energy source. Carbonization apparatus can be simplified, generation of dioxins or odor is prevented, and gas emitted from a to-be-processed object is used effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fundamental installation structure used for processing organic waste in which carbonization furnace and carbonization container are arranged in the vicinity of a combustion furnace.    Carbonization furnace (1)    Carbonization container (11)    Gas emission part (11c)    Organic waste (Y)    Waste oil (Z)
NOVELTY - This utility new type claims a methanol oxidation supply heat a hydrogen producing device, a raw material methanol tank, the raw material water tank, methanol tank, reactor, a fuel distributor, a fuel methanol evaporator, a methanol evaporator, the second fuel distributor, air chamber, reactor, a fuel distributor, a fuel methanol evaporator, a methanol evaporator, the second fuel distributor, air cavity from upper to lower in turn., further comprising hydrogen heat exchanger, a cooler, an air circulation system, a transformation absorbing device, this utility new type using methyl alcohol low temperature oxidation technology for methanol reforming hydrogen supply heat supply heat reaction, by low temperature oxidation catalyst, alcohol hydrogen mixed gas carry out oxidation reaction, reaction temperature is 600 degrees centigrade, not only a formaldehyde equal, and device operation more safe, waste heat, heat efficiency is high, can replace the electric heating, natural gas, diesel oil, heavy oil, coal heating equal heating device to achieve efficient, energy-saving, the purpose of environmental protection.
NOVELTY - This utility new type relates to sewage processing device, claims a cultivation waste water a gas cabinet, comprising cabinet body, said cabinet body middle part set has three phase separator, a three phase separator for the lower part cabinet body is divided into a water of reaction area and the upper part of the sludge precipitation zone, a middle part, a cabinet body top has set with marsh gas discharge pipe, upper part of three phase separator has set the water pipe, a sludge settling zone has set with water inlet tube. This utility new type at a low temperature low concentration and high concentration sewage or toxic when hardly-degradable industrial waste water comprises COD removing rate is high.
NOVELTY - This utility new type claims a one using a biomass fuel is a gas, comprising: a gas fuel for a gas generating system, equipped with a gas system a, a monitoring device for a fuel gas concentration in the conveying pipe is used for adjusting and adjusting device of biomass raw material distribution. This utility new type system by a gas fuel in the use of biomass is added with a monitoring device and adjusting device, a real time monitor for a gas fuel, and a gasification furnace inner distribution according to a monitoring result adjusting biomass raw material, so as to realize the self-combustion of control to avoid " burning through " equal uniform combustion of phenomenon. When gas in the fuel system using a biomass fuel gas is the production of a fuel gas content of reducing, a immediately, and adjustment is not in time for the quality of a finished product gas fuel cause influence. This utility new type comprises simple structure, convenient installation, manufacture cost low and the practicability is strong and equal.
NOVELTY - This utility new type claims a a lower sucking type biomass gasification furnace, burning biomass raw material for a gas fuel, comprising a, a side wall set with t for pneuma hole of upper furnace body, lower furnace body, a device used for a gas fuel is, for a said upper furnace body inner supply combustion-supporting gas of the pneuma.; for spreading a material level of material distributing device. This utility new type in a lower suction type biomass gasification furnace, by side-introducing combustion-supporting gas, solves the problem that the biomass material combustion uniformity problem is. By using combustion-supporting gas of a steam, reducing the nitrogen content in a gas fuel. By using steam isolation layer isolating atomphere and a biomass raw material pre-heating humidifying and biomass raw material for uniform distribution in upper inner furnace body by using a cloth. In addition, this utility new type further comprises simple structure equal.
NOVELTY - This utility new type relates to a low energy consumption of a refuse derived fuel preparation system, firstly using the aperture is 60-100 mm of garbage filter machine to carry out garbage filter, rear screen is a screen light object directly sending into waste shredding device, and screen after screen of a heavy object by a first separator after sending into waste shredding device, a sieve after a rear garbage by tearing a tearing by the first presser and the second presser two lever pressing is a RDF molding machine into a RDF; and can filter after carrying out compost or reducing water. This utility new type is a refuse derived fuel does not pass through a high temperature fermentation and drying procedure of the RDF, and the garbage can is a present day treatment, the system in a waste treatment process in a short period, low energy consumption, avoids the existing technology in garbage comprehensive processing a RDF of a period is long, the high energy consumption problem is.
NOVELTY - Stereoselectively reducing a carbonyl group comprised in an organic compound to a hydroxy group in a product of the same organic compound, comprises contacting the organic compound that comprises the carbonyl group with carbonyl reductases of fungus of the genus Penicillium.    USE - The method is useful for stereoselectively reducing carbonyl group comprised in an organic compound to hydroxy group in product of the same organic compound.    ADVANTAGE - The method is simple, cost effective and environment friendly and provides the product with improved yield and stereo-selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of a fungus of the genus Penicillium for stereoselectively converting a carbonyl group to a hydroxy group, where the carbonyl group is comprised in an organic compound.
NOVELTY - A hazel-mushroom cultivation medium comprises 40-41 %mass sawdust, 40-41 %mass fungus slag, 14-16 %mass wheat bran, 0.8-1 %mass bean flour, 0.8-1 %mass glucose, 0.3-0.5 %mass lime, 0.4-0.5 %mass protein peptide, 0.03 %mass huolisu, 0.03 %mass plant ash, and 0.02 %mass magnesium sulfate.    USE - Cultivation medium is used for hazel-mushroom shed-cultivation (claimed).    ADVANTAGE - The cultivation medium enables effective usage of fungus slag, which prevents destruction and consumption of forest resources, and environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for shed-cultivation of hazel mushroom, which involves preparing cultivation medium, adjusting moisture content to 70%, stirring, sealing in a bag, sterilizing for 10 hours at atmospheric pressure, carrying out aseptic inoculation, culturing at 23-27 degrees C for 60-70 days in dark, transferring when color is dark brown, adjusting relative humidity to 65-75% and temperature to 18-22 degrees C, maturing for 7-10 days, and harvesting.
NOVELTY - Seed coating agent comprises 1-2.25 pts. organic bio-fertilizer, 0.1-0.25 pts. humic acid, 0.05-0.15 pts. complex microbial broth, 0.01-0.025 pts. vermiculite and 1-3 pts. fixative.    USE - Used as a seed coating agent.    ADVANTAGE - The seed coating agent has strong pertinence, good commonality, disease resistance, insect prevention, and slow release properties; includes pure natural components, and is environmentally-friendly. The coating method is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for seed coating using the seed coating agent, comprising (i) mixing the fixative, complex microbial broth and to be coated seeds, to obtain film formed seed; and (ii) adding the film formed seed into organic bio-fertilizer, humic acid and vermiculite powder mixture, mixing well, and drying to obtain coated seeds.
NOVELTY - Method of deamination for producing biogas from alcohol residue involves (a) preheating alcohol residue, (b) heating the resulting alcohol residue at 3-10 degrees C, (c) subjecting the resulting alcohol residue to first steam treatment using deaminase, (d) removing ammonia gas and carrying out second steam treatment of resulting residue, and (e) performing the steps (c) and (d) to obtain product.    USE - The method is useful for producing biogas from alcohol residue (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for producing biogas from alcohol residue, which comprises (a) first heat exchanger, (b) second heat exchanger, (c) deaminase column, (d) wash gas column, and (e) compressor, where the first heat exchanger and second heat exchanger are connected to boiler, inlet and discharge pump, feed pump, and scrubber column, and outlet of compressor is connected to kettle type boiler.
NOVELTY - The device has a vertical hoisting machine (1) connected with a biomass rubbish underground material conveying stack that is connected to a storage hopper (2). The storage hopper is sealed with a taper and provided with a quantitative feeding mechanism (3). The quantitative feeding mechanism is connected with an equal volume biomass rubbish discharging pipe (4) that is connected with a bottom part of a double-head spiral propeller (5). The double-head spiral propeller and a hydraulic propeller (6) open a seal door (7) to convey rubbish to a biomass gasification furnace (8).    USE - Seal-type biomass rubbish quantitative feeding device.    ADVANTAGE - The device realizes biomass rubbish quantitative feeding function so as to achieve smooth and precise control of feeding process. The device has better sealing effect of a gasification furnace, and solves explosion safety problems and bottleneck problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of a seal-type biomass rubbish quantitative feeding device. '(Drawing includes non-English language text)'    Vertical hoisting machine (1)    Storage hopper (2)    Quantitative feeding mechanism (3)    Equal volume biomass rubbish discharging pipe (4)    Double-head spiral propeller (5)    Hydraulic propeller (6)    Seal door (7)    Biomass gasification furnace (8)
NOVELTY - An ether ester methanol fuel comprises 60-80 wt.% methanol, 10-20 wt.% lower alcohol, 5-15 wt.% ether, and 5-12 wt.% ester. The lower alcohol is ethanol, propanol, glycerol and/or isobutanol mixture. The ether is ethyl tertiary butyl ether, t-amyl methyl ether, ethyl t-amyl ether and/or diisobutyl ether mixture. The ester is ethyl acetate, diethylene glycol fatty acid ester, dibutyl phthalate and/or propyl nitrate mixture.    USE - Ether ester methanol fuel used for car engine.    ADVANTAGE - The fuel is environment-friendly, solves alcohol fuel power shortage and corrosion swelling problems without modifying car engine, it can directly replace gasoline, and it has greatly reduced emissions and low cost.
NOVELTY - A high clean diesel oil emulsifier comprises 20-40 wt.% vegetable oil, 15-30 wt.% mixed alcohol, 10-15 wt.% fatty acid methyl ester, 5-15 wt.% fatty acid, 3-10 wt.% organic amine, 3-10 wt.% inorganic base, 3-10 wt.% light oil, and 2-5 wt.% acetone.    USE - High clean diesel oil emulsifier used for vehicle and ship.    ADVANTAGE - The emulsifier has good stability, quality and long-term stratification.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) diesel oil emulsifier comprising adding vegetable oil into reactor while stirring, mixing with remaining raw materials except organic amine, stirring for 15 minutes, adding organic amine, continuously stirring for 35 minutes; and    (2) preparation of high clean diesel oil comprising mixing 65-85 wt.% diesel, 10-25 wt.% water and 3-10 wt.% emulsifier, and stirring according to clean diesel oil national standards.
NOVELTY - Preparation of biomass fuel granule comprises softening agriculture and forestry waste raw materials, grinding, separating fibers, drying, and granulating.    USE - Method for preparing biomass fuel granule (claimed).    ADVANTAGE - The fuel reduces environment pollution, increase heat and produces less dust.
NOVELTY - The hydrogen generator has electrodes, which are connected to a filling cork. A polypropylene homopolymer is deposited in a wall, which has thickness of 5 millimeter, where an electrolyte potassium hydroxide is utilized with a volume of 22.5 liters. A threaded stainless steel rod has a diameter of 8 millimeter and a length of 30 centimeter, where a transparent tube is installed with a lateral support.    USE - Hydrogen generator for combustion motors.    ADVANTAGE - The electrodes are connected to a filling cork, where polypropylene homopolymer is deposited in a wall and an electrolyte potassium hydroxide is utilized, and thus ensures increased resistance and prevents the damage.
NOVELTY - A container box-type biodiesel production apparatus consists of cooking oil reservoir, methanol reservoir, potassium hydroxide reservoir, mixer, reactor, separator, biodiesel reservoirs (a) and (a'), glycerin reservoirs (b) and (b'), connectors (c) and (c'), and container box, where biodiesel reservoir (a') and glycerine reservoir (b) are connected between the separator and the biodiesel reservoir (a).    USE - Container box-type apparatus is used for production of biodiesel.    ADVANTAGE - The container box-type apparatus is safe to use, and is not affected by external environment.
NOVELTY - Method for segregating biomass, involves (a) adding 8-70 parts mass, preferably 10-10000 parts mass alkaline water with respect to solid content of 100 mass parts of herbal biomass, and heating mixture to obtain primary alkaline treated biomass, (b) soaking primary alkaline treated biomass in 6-60 %mass alkaline solution at 0-50 degrees C to obtain secondary alkaline treated biomass, and (c) obtaining secondary alkaline treated biomass, and separating glucan from mixture containing lignin, and xylan.    USE - The method is useful for segregating biomass (claimed).    ADVANTAGE - The method enables to segregate component of glucan, xylan, and lignin contained in plant-derived biomass with the high recovery rate.
NOVELTY - Manufacture of liquid fuel (5) involves decomposing a fat and oil-containing waste liquid (1) by a biochemical reaction and obtaining a solid higher fatty acid (3), and esterifying the higher fatty acid.    USE - Manufacture of liquid fuel (claimed) from combined-purification tank sludge and wastewater from manufacturing oil-and-fat product.    ADVANTAGE - The method enables manufacture of liquid fuel with prevention of byproduct of glycerol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (10) for manufacturing liquid fuel, which comprises a decomposition unit (12) and an esterification unit (14).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus. (Drawing includes non-English language text)    Fat and oil-containing waste liquid (1)    Solid higher fatty acid (3)    Liquid fuel (5)    Apparatus (10)    Decomposition unit (12)    Esterification unit (14)
NOVELTY - Uronema sp. KGE 3 strain, is new.    USE - The strain is useful for producing beta -carotene from waste water containing mine drainage and cattle manure (all claimed), and bio-diesel.    ADVANTAGE - The strain has resistance to heavy metal, and high content of palmitic acid, palmitoleic acid, oleic acid, linoleic acid, and gamma -linoleic acid.
NOVELTY - Pseudo hydrotalcite catalyst (I), is claimed.    USE - The catalyst is useful producing glycerol carbonate by reacting glycerol (derived from biodiesel or its by-products) with element (all claimed).    ADVANTAGE - The catalyst has high specific surface area, thermal stability, weak Lewis acid sites and base nature and mechanical strength, and improves purity and quality of glycerol carbonate.    DETAILED DESCRIPTION - Pseudo hydrotalcite catalyst of formula (((M12+)1-X(M22+)1+X(OH)2)((A(n-))2/n)) (I), is claimed.    M1, M2 = divalent metal element of IIA group or IIB group elements;    A = carbonate ion, sulfate ion, nitrate ion, hydroxy ion, iodine ion or fluoride ion as interlayer;    n = 1 or 2 oxidation number of interlayer; and    x = 0.3-0.7.    An INDEPENDENT CLAIM is also included for producing (I), comprising (i) dissolving divalent metal element precursor (M1 and M2) into distilled water to obtain precursor solution, adding alkali metal hydroxide in the precursor solution, and processing to obtain precipitate, (ii) filtering the precipitate, drying at 50-100 degrees C, and primarily sintering at 100-3000 degrees C under air, (iii) dispersing the primarily sintered body with alcohol binder in aqueous alcohol solution, and hydrothermally reacting at 80-150 degrees C, (iv) molding the obtained product, and secondarily sintering at 100-3000 degrees C under air, and (v) dispersing the secondary sintered body with anions compound (A), and stirring at 90-120 degrees C for producing hydrotalcite catalyst.
NOVELTY - The furnace has a gasification furnace hearth that is divided into pneumatic reforming zone (A). A pneumatic reforming zone comprised in the same horizontal plane is uniformly equipped with three branches of plasma torch (2). The side face of a gasification portion is connected with a feeding system (1). An air inlet is equipped in the side face of gasification portion whose bottom is comprised with garbage and waste separating residue zone. A fire grate (5) is equipped with the middle of the plasma portion (6).    USE - Integrated garbage plasma gasification furnace.    ADVANTAGE - The refractory material dosage is reduced, and improved economical efficiency is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the integrated garbage plasma gasification furnace.    Feeding system (1)    Plasma torch (2)    Fire grate (5)    Plasma portion (6)    Pneumatic reforming zone (A)
NOVELTY - The device has the furnace housing (10) that is connected with a foundation bed (20). A furnace cover (40) is connected with a water pump (50) and multiple nozzles (42). A second cavity portion (60) is formed between the furnace cover and furnace housing. A ground portion (30) is set with a water storage tank (31). The water storage tank is located in the foundation bed formed with a water hole (21). The two ends of water pump are connected with water storage tank and first cavity portion (41) through respective pipelines (70,80).    USE - Device for cooling biomass gasification furnace.    ADVANTAGE - The safety of the operator is improved. The cooling efficiency of the cooling device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the device for cooling biomass gasification furnace.    Furnace housing (10)    Foundation bed (20)    Water hole (21)    Ground portion (30)    Water storage tank (31)    Furnace cover (40)    Cavity portions (41,60)    Nozzle (42)    Water pump (50)    Pipelines (70,80)
NOVELTY - A bio-diesel comprises 30-45 wt.% peanut oil, 30-45 wt.% palm oil, 10-30 wt.% turpentine, 5-10 wt.% alkane and 0.2-0.5 wt.% ferrocene.    USE - Bio-diesel (claimed).    ADVANTAGE - The bio-diesel reduces exhaust emission by 50-60%, and is manufactured by simple, economical and environmentally-friendly process with high yield and reduced energy consumption.
NOVELTY - A biodiesel production by palm oil comprises taking 60 wt.% palm oil and 40 wt.% methanol, adding 5 wt.% of 98 vol.% industrial sulfuric acid and 1 wt.% phosphoric acid, heating at 60-70 degrees C, stirring for 1-2 hours, precipitating for 12-24 hours, adding 100:1 volume ratio of methanol and sodium hydroxide solution, heating at 60-70 degrees C, stirring 1-2 hour, precipitating for 12- 24 hours, taking supernatant, adding 3-10 wt.% hydrogen peroxide and 0.5-2 wt.% benzoyl peroxide, stirring for 0.5-2 hours, heating at 80-90 degrees C, depositing, and filtering.    USE - Biodiesel production by palm oil (claimed).    ADVANTAGE - The biodiesel has good low temperature engine starting performance.
NOVELTY - Alcohol-based fuel oil comprises 70-90 %mass methanol, 3-15 %mass xylene, 3-8 %mass acetone, 2-5 %mass coal tar, 0.2-2 %mass phenol or methylphenol and 0.1-10 %mass magnesium.    USE - Alcohol-based fuel oil (claimed).    ADVANTAGE - The alcohol-based fuel oil having high calorific value of 37.6-41.8 MJ/kg and stability, is manufactured with reduced fuel consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based fuel oil.
NOVELTY - A vehicle alcohol-based fuel comprises 55-70 wt.% No. 93 gasoline, 10-15 wt.% methanol, 0.2-0.5 wt.% ethanol, 3-15 wt.% combustion improver, 0.1-0.5 wt.% additive, 0.003-0.1 wt.% speed combustion supporting agent, 1-2 wt.% bio-oil and 1 wt.% anti-explosion liquid.    USE - Vehicle alcohol-based fuel.    ADVANTAGE - The fuel is low-cost, energy efficient, environment-friendly and has excellent performance.
NOVELTY - A pour point depressant comprises 50-70 %mass polymaleic acid-acrylamide-styrene, 10-15 %mass surfactant and 15-40 %mass poly acid amide.    USE - Pour point depressant is used for bio-diesel.    ADVANTAGE - The pour point depressant has excellent solubility and low-temperature flow performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of pour point depressant.
NOVELTY - A methanol fuel additive comprises 5-10 pts. wt. cyclohexanone peroxide, 30-35 pts. wt. hydrazine t-butyl acetic acid, 10-15 pts. wt. intermediate, 5-10 pts. wt. antioxidant corrosive additive and 5-15 pts. wt. oxygen-containing compound combustion improver.    USE - Methanol fuel additive.    ADVANTAGE - The fuel has good cleaning effect, increased engine air intake resistance, decreased inflatable gas mixture oil coefficient, reduced methanol to metal corrosion rate, and extends vehicle life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol fuel additive comprising taking antioxidant corrosive additive and cyclohexanone peroxide, mixing, filtering, adding oxygen-containing compound combustion improver, stirring, adding remaining raw materials, and mixing.
NOVELTY - A biodiesel compound additive comprises 20-30 pts. wt. cetane improver, 14-25 pts. wt. low temperature flow improver, 6-12 pts. wt. corrosion inhibitor, 4-8 pts. wt. antioxidant and 7-15 pts. wt. detergent.    USE - Biodiesel compound additive.    ADVANTAGE - The additive has synergetic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel compound additive comprising taking raw materials, and stirring at rate of 100-200 revolutions/minute.
NOVELTY - An additive comprises 18-31 wt.% 1-imidazole-octyl-3-bromide, 15-30 wt.% 3-oxa-9-azabicyclo(3.3.1)nonane-7-one, 15-25 wt.% potassium methoxide, 13-24 wt.% 1-hexyl-4-piperidine amine, 10-21 wt.% hexenyl isobutyrate and 9-20 wt.% 2-amino-4-methylthiazole.    USE - Additive is used in alcohol-based fuel (claimed).    ADVANTAGE - The alcohol-based fuel provided using the 0.1-0.6 wt.% additive has reduced generation of particulate material during combustion.
NOVELTY - Emulsifying emulsion, involves introducing diesel oil into Venturi tube at a pressure of 0.35 MPa and then transferring to a diffuser, passing the diffused product into a homogeneous reactor and then adding alcohol and water in a ratio of 1:3-1:5, circulating the mixture in the homogeneous reactor through a circulation tube for 60 minutes to obtain stable and transparent product of alcohol and diesel oil.    USE - The method is useful for emulsifying emulsion (claimed).    ADVANTAGE - The method is capable of emulsifying emulsion in an economical manner.
NOVELTY - A biomass briquette comprises 45-55 wt.% coal, 35-45 wt.% tobacco stalks, 5-7 wt.% ash, 2-5 wt.% bentonite and 0.2-0.6 wt.% additive.    USE - Biomass briquette (claimed).    ADVANTAGE - The biomass briquette can be easily molded and has high desulfurization rate, and is prepared with reduced coal consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass briquette.
NOVELTY - A biomass solid fuel is obtained by molding composition comprising 10-20 pts. wt. limonene, 10-15 pts. wt. 1-11C monohydric alcohol, 3-10 pts. wt. gasoline, 15-25 pts. wt. wastewater, 20-30 pts. wt. wood powder and 3-5 pts. wt. binder.    USE - Biomass solid fuel (claimed).    ADVANTAGE - The biomass solid fuel does not contain parathion, and is manufactured with reduced energy consumption.
NOVELTY - Manufacturing biomass fuel involves adding raw material into a reaction container to dry for 20-30 minutes, crushing the dried material to obtain powder, and adding biological crude oil to obtained powder.    USE - Method for manufacturing biomass fuel (claimed).    ADVANTAGE - The method improves the processing efficiency of biomass fuel.
NOVELTY - Preparation of biomass fuel involves crushing raw material comprising 95-98 pts. wt. straw, 0.1-0.2 pt. wt. oxidant and 0.4-0.5 pt. wt. slagging agent, drying, controlling moisture content of the mixture at less than 5%, adding antioxidant and slag-forming agent, stirring, and granulating to particle size of 1-4 mm. The particle size of pulverized straw is 5-10 mm. The particle size of slagging agent is 70-120 mesh.    USE - Preparation of biomass fuel (claimed).    ADVANTAGE - The biomass fuel is prepared with low combustion efficiency.
NOVELTY - Compact biomass briquette comprises 4.7 pts. wt. almond shell, 2.9 pts. wt. cottonwood, 5.6 pts. wt. rubber, 2.1 pts. wt. birch wood, 3.2 pts. wt. oil seed meal, 0.7 pts. wt. slag and 1.5 pts. wt. rice stick powder.    USE - Compact biomass briquette.    ADVANTAGE - The compact biomass briquette significantly increases combustion rate and thermal efficiency.
NOVELTY - A biomass briquette comprises 2.5 pts. wt. peanut shell, 1.9 pts. wt. Davidia involucrata sawdust, 2.6 pts. wt. peach wood, 3.1 pts. wt. elm wood, 2.9 pts. wt. palm shell, 0.9 pts. wt. magnesium slag and 1.9 pts. wt. soybean straw powder.    USE - Biomass briquette (claimed).    ADVANTAGE - The biomass briquette has excellent durability and thermal combustion efficiency.
NOVELTY - Biomass forming fuel comprises 3.1 pts. wt. walnut, 1.2 pts. wt. Robinia wood chip, 1.8 pts. wt. pine chip, 2.8 pts. wt. ash wood, 0.4 pts. wt. ammonium dihydrogen phosphate, 1.6 pts. wt. corn core and 2.2 pts. wt. flax straw stick powder.    USE - Biomass forming fuel.    ADVANTAGE - The biomass forming fuel significantly improves the thermal efficiency and combustion rate.
NOVELTY - A composite solid fuel comprises 5.6 pts. wt. Cornus officinalis seeds, 6.1 pts. wt. Syzygium sawdust, 0.7 pt. wt. diammonium phosphate, 2.8 pts. wt. sandalwood debris, 3.2 pts. wt. ash wood, 1.4 pts. wt. pine needles and 2.8 pts. wt. pulverized corn stalk.    USE - Composite solid fuel (claimed).    ADVANTAGE - The composite solid fuel has excellent thermal combustion efficiency for long period of time.
NOVELTY - Method for degrading food waste involves inoculating microbial inoculum into the solid organic food waste along with the carrier material, where the weight of the liquid microbial inoculum is 10-200 % weight of the carrier material.    USE - Method for degrading food waste (claimed).    ADVANTAGE - The method enables to degrade food waste by effectively reducing the operation load of solid organic food waste, and thus improves the efficiency of waste degradation by decomposing bacteria. The method degrades food waste in an economical manner.
NOVELTY - A recombinant microorganism conversion to carbon source for producing biodegradable polymer and biomass fuel is performed by using glycerol-containing gene and gene recombinant microorganism ferment of polyhydroxyalkyl ester synthetase gene to construct recombinant DNA, culturing gene recombinant microorganism in glycerol, inducing gene recombinant microorganism expression and glycerol-containing enzyme gene to obtain polyhydroxyalkyl ester biodegradable polymer and ethyl alcohol biomass fuel, and separating polyhydroxyalkyl ester and ethyl alcohol.    USE - Recombinant microorganism conversion to carbon source for biodegradable polymer and biomass fuel.    ADVANTAGE - The process has high efficiency, reduces production cost, removes waste, and is environment-friendly.    DETAILED DESCRIPTION - A recombinant microorganism conversion to carbon source for producing biodegradable polymer and biomass fuel is performed by using glycerol-containing gene and gene recombinant microorganism ferment of polyhydroxyalkyl ester synthetase gene to construct recombinant DNA, culturing gene recombinant microorganism in glycerol, inducing gene recombinant microorganism expression and glycerol-containing enzyme gene to obtain polyhydroxyalkyl ester biodegradable polymer and ethyl alcohol biomass fuel, and separating polyhydroxyalkyl ester and ethyl alcohol in which recombinant microorganism is greater than or equal to 30 (w/w)% of polyhydroxyalkyl ester product, and glycerol is greater than or equal to 90 (w/w)%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of (pARD33) expression and (pBHB2) double-plastid.
NOVELTY - RNA isothermal amplification-based avian influenza virus H7N9 nucleic acid detection reagent kit comprises (i) virus preservation solution, nucleic acid extract, a washing liquid and H7N9 reaction liquid, H7 test solution, N9 test solution, serine acetyltransferase (SAT) enzyme solution, H7N9 positive control, H7N9 negative control, and multi-reagent bottle or sealed tube; and (ii) H7 test solution and N9 test solution, includes pair of upstream primer, and 5' end downstream primer of T7 promoter sequence, and a separate and concentrated pack of reagent bottle or packaged tube.    USE - The reagent kit, primer or probe are useful in the detection of presence or absence of H7N9 in avian feces and other secretions or human nose and throat secretions and other human samples (claimed).    ADVANTAGE - The reagent kit has high specificity, high sensitivity, and rapid detection effect; is environmental friendly; and diagnosis H7N9 during early stage of infection.    DETAILED DESCRIPTION - RNA isothermal amplification-based avian influenza virus H7N9 nucleic acid detection reagent kit comprises (i) virus preservation solution, nucleic acid extract, a washing liquid and H7N9 reaction liquid, H7 test solution, N9 test solution, serine acetyltransferase (SAT) enzyme solution, H7N9 positive control, H7N9 negative control, and multi-reagent bottle or sealed tube; and (ii) H7 test solution and N9 test solution, respectively includes pair of upstream primer, and 5' end downstream primer of T7 promoter sequence, and a separate and concentrated pack of reagent bottle or packaged tube, where the both ends of the primer are covalently labeled with a fluorescent dye, and a quenching agent of single-stranded nucleic acid probes, and nucleic acid extract includes magnetic beads and capture probes.
NOVELTY - A biomass polysaccharide grafted polymer chain method comprises reacting polysaccharide and end-functionalized polymer functional group or hydrogen functional group.    USE - Biomass polysaccharide grafted polymer chain method (claimed).    ADVANTAGE - The method is simple and has mild reaction conditions.
NOVELTY - The system has a conversion fan that is connected with a gas storage device (9). A second secondary chamber (3) is connected with a lower suction type gasification furnace housing (4). A discharge pipe (5) is connected with a waste heat recovery device (6) connected to water level meter (21). A gas storage portion (27) is connected with a spiral dust-removing washing device (7) set with lower end connected to a dust removing valve (26). The lower end of the waste heat recovery device is connected with a hydrogen device (13).    USE - System for supplying heat to biomass fixed bed gasification furnace.    ADVANTAGE - The temperature of the gasification furnace is increased to 950-1100 degrees C. The heating efficiency of the gasification furnace is improved. Environmental protection of the furnace is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for supplying heat to biomass fixed bed gasification furnace.    Second secondary chamber (3)    Lower suction type gasification furnace housing (4)    Discharge pipe (5)    Waste heat recovery device (6)    Spiral dust-removing washing device (7)    Gas storage device (9)    Hydrogen device (13)    Water level meter (21)    Dust removing valve (26)
NOVELTY - Producing soybean oil biodiesel comprises using triphenyltetrazolium chloride as indicator for screening Saccharomyces cerevisiae, using sugar and sweet sorghum stalk juice for fermentation for 63 hours and 45 hours, where the sweet sorghum is natural crops, complexing, using ultraviolet mutagenesis process, selecting and breeding mutant strain of NY-06 under optimum fermentation temperature and pH value.    USE - The method is useful for producing soybean oil biodiesel (claimed).    ADVANTAGE - The method is simple, is convenient to operate, is suitable for daily production, and has good popularization prospect.
NOVELTY - A catalyst is obtained by mixing metal halide as catalyst precursor, and carbon-based material as active ingredient, and has particle size of 60-100 mesh. The content of carbon-based material is 6-30 %mass.    USE - Catalyst is used for coal gasification for producing methane, hydrogen and syngas (all claimed).    ADVANTAGE - The catalyst has excellent gaseous product conversion rate, improves the content of methane and improves the utilization of coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of catalyst.
NOVELTY - (6R,7R)-7-Amino-3-((Z)-2-(4-methylthiazol-5-yl))ethenyl-8-oxo-5-thia-1-azabicylo(4.2.0)oct-2-ene-2-carboxylic acid (7-ATCA) or its active ester or hydrochloride salt is dissolved in methylene chloride and organic base is added dropwise at -5 degrees C to 15 degrees C. The contents are reacted and extracted with water. A hydrophilic solvent is added to the aqueous phase and decolored. Hydrochloric acid is added to the obtained solution at 10-35 degrees C and cefmenoxime hydrochloride is crystallized.    USE - Synthesis of cefmenoxime hydrochloride (claimed).    ADVANTAGE - The synthesis method produces cefmenoxime hydrochloride by a single solvent condensation reaction, with high conversion rate and convenient solvent recovery. Since cefmenoxime hydrochloride is directly crystallized, the crystals are easy to separate and dry, and do not require a special separating device. Cefmenoxime hydrochloride is manufactured economically by a simple process with improved productivity.
NOVELTY - An alternating current plasma torch comprises a reactor, a ground electrode having a bottle shape, an insulating layer, an insulating cover, high-voltage electrode and gas ring. An upper end of the ground electrode is connected to lower end of insulating cover, and is provided with nozzle. The ground electrode is present in contact with insulating layer. The gas ring is arranged in lower end of ground electrode. The high-voltage electrode is mounted on gas ring.    USE - The alternating current plasma torch is useful for producing synthesis gas including air, methane and carbon dioxide (all claimed).    ADVANTAGE - The alternating current plasma torch is capable of producing synthesis gas at a voltage amplitude of 2-20 kV and current amplitude of 0.1-10 A, and has improved working efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis gas including air, methane and carbon dioxide operated at three different modes.
NOVELTY - A hydrogen-production system comprises a cartridge, a controller, a hydrogen pressure sensor, a condenser, hydrogen fuel cells, a reaction chamber, a storage chamber, a storage cartridge containing magnesium powder, water and additives, a functional cartridge operated at direct current voltage of 12 V, a catalytic electrode connected to cartridge via a control circuit, and an outlet connection. The controller is connected to sensor, hydrogen fuel cells and catalytic electrode through the control circuit. A hydrogen pipe is connected with the storage chamber.    USE - The system is useful for producing hydrogen from water (claimed).    ADVANTAGE - The system is lightweight, and produces hydrogen from water in an efficient and environmentally-friendly manner.
NOVELTY - Recovering nutrients from biogas slurry using adsorbent, comprises: (a) carrying out solid-liquid separation of biogas slurry by sequentially passing through 5A molecule sieve, titanium dioxide and kaolin for 10-20 minutes, 50-60 minutes and 15-25 minutes respectively with an adsorption temperature of 25-35 degrees C; (b) utilizing the 5A molecule sieve desorption concentrate for preparing liquid nitrogen fertilizer, and utilizing the kaolin desorption concentrate for preparing liquid organic fertilizer; and (c) utilizing the remaining adsorbent waste for preparing soil modifying agent.    USE - The method is useful for recovering nutrients from biogas slurry using adsorbent (claimed).    ADVANTAGE - The method adopts selective adsorbent for adsorbing different nutrient substance.
NOVELTY - Method for disposing domestic wastewater involves screening household wastewater to remove sand, harmful metals and non-fermentable ingredients, placing the screened wastewater in an enclosed space, introducing domestic wastewater into garbage site, flooding domestic waste, adding fermenting mold, fermenting, removing precipitate, and generating liquid manure.    USE - Method for disposing domestic wastewater for use in manufacture of fertilizer used in agricultural.    ADVANTAGE - The method enables efficient disposing of domestic wastewater by simple method.
NOVELTY - Use of microalgae photobioreactor is claimed for wastewater treatment and biodiesel production involves treating sewage busing multilayer tandem open reactor, separating effluent using membrane bioreactor, performing lipid-induced accumulation using spiral pipe sealed reactor, and harvesting lipid using funnel to obtain lipid pool.    USE - Use of microalgae photobioreactor for wastewater treatment and biodiesel production.    ADVANTAGE - The process is environment-friendly because sewage treatment step is highly efficient in which product is oxygen, and irritating and malodorous gas are reduced. The spiral pipe sealed reactor has high energy utilization rate, promotes microalgae photosynthesis, reduces occupied area, and increases space utilization rate.
NOVELTY - Biogas slurry preparation involves heating pig liquid at 70-100 degrees C for 10-25 minutes. The heated mixture is added with 15-25g/l zeolite. The mixture is filtered for 20-30 hours. The mixture is added with inoculated micro-algae and then heated at 24-26 degrees C. The mixture is cultured for 10-15 days. The mixture is separated, and then purified.    USE - Method for preparing biogas slurry (claimed).    ADVANTAGE - The method enables to prepare biogas slurry in a cost-effective manner.
NOVELTY - The system has a tank floating cover whose side wall is provided with a vertical guide rail. The upper end opening of a tank portion is provided with a chain wheel along the circumferential direction. An upper pulley is connected with the tank floating cover. The tank portion is provided with an annular water sealing groove. An annular water seal tank is connected with tank portion. The lower portion of tank portion is set with an air inlet. The top portion of tank floating cover is provided with a human hole, a discharge hole and a vent hole.    USE - Cultivation farm sewage processing system.    ADVANTAGE - The sewage processing effect of sewage processing system is increased so that the cultivation farm waste water is processed efficiently. Hence the methane is produced easily at the same time of sewage treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cultivation farm sewage processing system.    Grid pool (1)    Water collecting stirring pool (2)    Primary regulating pool (4)    Anoxic pool (7)    Acidification tank (16)
NOVELTY - The municipal sludge treatment process involves: (1) anaerobic digestion of municipal sludge; and (2) aerobic fermentation of anaerobically digested sludge at high temperature.    USE - Method is useful for treatment of municipal sludge, which is useful to prepare nutrient soil and bio-organic fertilizer (all claimed).    ADVANTAGE - The method completely reduces municipal sludge, reduces environmental pollution, and increases efficiency of recycling municipal sludge. The treated municipal sludge increase soil organic matter and improves soil structure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) usage method of processed municipal sludge to obtain nutrient soil, where the nutrient soil has organic matter content of 45%, nitrogen-phosphorus-potassium total nutrient content of 5%, and heavy metal concentration pollution limit lower than in urban construction industry sludge; and (2) a bio-organic fertilizer prepared by (1) preparing nutrition soil, crushing and sieving and (2) culturing Lactobacillus acidophilus, Bacillus subtilis and Aspergillus niger in nutrient soil to obtain bio-organic fertilizer.
NOVELTY - The preparation method of organic matrix involves: (1) mixing mushroom, cotton seed hulls, crushed corn stover, straw, sawdust and peat in fermentation cement pond, adding organic fertilizer fermentation bacteria, covering with plastic film and sealing, adding water to reduce evaporation and fermenting for 2-3 days, then fermenting at a temperature of up to 70 degrees C for 15 days, adding water and then fermenting for 10-15 days; and (2) air-drying the fermented substrate to have a moisture content of 16-18%, and pulverizing to particle size of 12-20 mm.    USE - Method is useful for preparing organic matrix for cucumber.    ADVANTAGE - The method enables easy preparation of organic matrix with small product density, improved quality and excellent fertilizer effect and that increases yield of cucumber.    DETAILED DESCRIPTION - The preparation method of organic matrix involves: (1) mixing 12-16 pts. wt. mushroom, 20-24 pts. wt. cotton seed hulls, 5-10 pts. wt. crushed corn stover, 4-8 pts. wt. straw, 12-18 pts. wt. sawdust and 10-12 pts. wt. peat in fermentation cement pond, adding 1-3 wt.% organic fertilizer fermentation bacteria, covering with plastic film and sealing, adding water to reduce evaporation and fermenting for 2-3 days, then fermenting at a temperature of up to 70 degrees C for 15 days, adding water, then fermenting for 10-15 days, and stopping fermentation when the matrix has pH of 6.8-7.2 and EC value of 0.90-1.1 mS/cm; (2) air-drying the fermented substrate to have a moisture content of 16-18%, pulverizing to particle size of 12-20 mm, and then air-drying granules until the water content is less than 4%, and then pulverizing to a particle size of less than 8 mm; and (3) screening, cleaning and winnowing the organic matrix to produce particles smaller than 6 mm.
NOVELTY - A closed fermentation organic fertilizer supplement transfusion stirring device comprises fermentation groove (1) having stirrer (2) and inlet tube, supplement liquid tank (5), supplement tube, air fan, infusion pipe, liquid supply pump (4) having liquid outlet pipe, speed-reducing motor (3), rotating shafts, bearing, oil seal, through-hole, fixing stirring blade and distribution nozzle.    USE - Closed fermentation organic fertilizer supplement transfusion stirring device.    ADVANTAGE - The device regulates pH during operation, thus providing suitable fermentation environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of closed fermentation organic fertilizer supplement transfusion stirring device.    Fermentation groove (1)    Stirrer (2)    Speed-reducing motor (3)    Liquid supply pump (4)    Supplement liquid tank (5)
NOVELTY - Production of selenium-containing liquid fertilizer comprises weighing 1-2 pts. wt. pig, sheep, and cattle manure and 8-15 pts. wt. water, mixing, naturally storing more than 6 months, and filtering through 100-300 meshes sieve; and taking 1 pt. wt. sodium selenite, adding 45-55 pts. wt. filtrate, stirring, and naturally fermenting for 15-35 days at 15-35 degrees C.    USE - Method for producing selenium-containing liquid fertilizer (claimed).    ADVANTAGE - The fertilizer coverts inorganic selenium to organic selenium and overcomes environmental pollution of traditional inorganic selenium selenite. The method is simple and low production cost.
NOVELTY - Method of preparing fertilizer for orange tree, involves cutting plant straw, composting and fermenting cut plant straw, grass peat and animal excrement for 50-60 days, mixing fermented material with urea, ammonium sulfate, calcium superphosphate, ammonium phosphate, potassium chloride, borax, ammonium molybdate, manganese sulfate, zinc sulfate and magnesium sulfate, pulverizing the mixture to obtain powdered fertilizer, drying the fertilizer at 65-75 degrees C and granulating to obtain the granular fertilizer.    USE - The method is useful for preparing fertilizer for orange tree (claimed).    ADVANTAGE - The fertilizer is easy to be absorbed by the orange tree and reduces soil pollution.
NOVELTY - A fertilizer comprises 10-12 pts. wt. straw, 10-15 pts. wt. ash, 5-10 pts. wt. Astragalus sinicus, 8-10 pts. wt. Sesbania exaltata, 2-5 pts. wt. lettuce, 2-3 pts. wt. phosphobacteria, 2-3 pts. wt. potassium-solubilizing bacteria and 2-5 pts. wt. perlite.    USE - Fertilizer (claimed).    ADVANTAGE - The fertilizer is non-toxic and environmentally-friendly, and has low volatility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer.
NOVELTY - A fertilizer comprises 60-80 pts. wt. Actinomyces, 80-100 pts. wt. silicate-solubilizing bacteria, 25-45 pts. wt. Bacillus subtilis, 25-35 pts. wt. urea, 4-6 pts. wt. borax, 30-50 pts. wt. photosynthetic bacteria and 80-110 pts. wt. Trichoderma.    USE - Fertilizer (claimed).    ADVANTAGE - The fertilizer effectively improves soil physical properties such as soil aggregate, reduce soil compaction and improves water-retention property, and provides suitable environment for growth of probiotics.
NOVELTY - A biological fertilizer comprises plant extract residue, plant extract decomposed residue, and microorganism.    USE - Biological fertilizer is useful for preventing and treating soil-borne diseases and soil pests.    ADVANTAGE - The biological fertilizer can be prepared with high nutritional value and reduced energy consumption in an economical manner, does not contain wastewater, emissions, carbon residues, any chemical pesticides and hormones, is environmentally-friendly, prevents soil-borne diseases with good control effect, and has excellent physical and chemical properties and microbial communities structure, high efficiency and long-lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological fertilizer, which involves adding plant extract residue to a reactor and then stirring, adding carbon and nitrogen in a ratio of 25:1-30:1 to the reactor, uniformly mixing, adding carbon and phosphorus in a ratio of 80:1-120:1 to the mixture, stirring the mixture with a moisture content of 45-65% and a pH value of 6.8-7.8, adding decomposed microbial agent to the mixture and then fermenting at 50-70 degrees C for 15-21 days to obtain a fermented material, adding Bacillus amyloliquefaciens and plant extract decomposed residue to the fermented material, and fermenting.
NOVELTY - Preparation of organic fertilizer involves adding chicken manure to a fermentation tank, composting, adding microbial functional bacteria, water retention agent, nitrogen fertilizer, phosophate fertilizer, potassium fertilizer and trace element fertilizer, stirring, providing resultant product into an oven, drying, grinding into powder, and packaging.    USE - Preparation of organic fertilizer used in tea tree planting.    ADVANTAGE - The method enables simple, economical and effective preparation of organic fertilizer. The organic fertilizer effectively improves survival rate of seedlings.
NOVELTY - A N-heterocyclic ring compound (I), (II), (III) or (IV) is prepared charging metal catalyst, o-substituted aniline compound and carboxylic acid or carboxylic acid ester to a reaction container, vacuumizing, filling oxygen or air, sealing, heating to 60-150 degrees C and reacting for 8-40 hours; cooling reaction system to room temperature, washing with water or with saturated brine, then extracting, drying, decompressing and distilling to remove organic solvent; and purifying crude product by column chromatography. The metal catalyst is iron catalyst or copper catalyst.    USE - Method of preparing N-heterocyclic ring compound (claimed).    ADVANTAGE - The method has mild reaction condition, high selectivity and yield of product, and is green and environment-friendly and suitable for industrialization. Further, the method utilizes copper or iron catalyst which is low in cost and easy to obtain.    DETAILED DESCRIPTION - Preparation of N-heterocyclic ring compound of formula (I), (II), (III) or (IV) comprises charging metal catalyst, o-substituted aniline compound and carboxylic acid or carboxylic acid ester to a reaction container, vacuumizing, filling oxygen or air, sealing, heating to 60-150 degrees C and reacting for 8-40 hours; and after finishing reaction, cooling reaction system to room temperature, washing with water or with saturated brine, then extracting, drying, decompressing and distilling to remove organic solvent to obtain crude product, and purifying crude product by column chromatography. The metal catalyst is iron catalyst or copper catalyst.    R=H, Me or Br;    R1=H or Me; and    R2=1-3C alkyl, phenyl, methylphenyl, 3-methoxyphenyl, p-hydroxyphenyl, p-aminophenyl, 3-chlorophenyl, p-bromophenyl, o-iodobenzyl, 1-naphthyl, 2-naphthyl, pyridyl, thienyl or 3-indolyl.
NOVELTY - Processing of glycyrrhizic acid involves extracting licorice in boiling water, separating using resin column, washing licorice component of resin column with water, removing bitter quality, spray-drying, obtaining licorice cream, washing licorice component of resin column using alcohol, separating, refining and obtaining glycyrrhizic acid.    USE - Processing of glycyrrhizic acid (claimed).    ADVANTAGE - The method enables environmentally-friendly processing of glycyrrhizic acid by extracting licorice with high extraction rate within short period of time, with high resource utilization.
NOVELTY - A mushroom is cultivated by mixing sawdust and water, stirring uniformly, placing into culture flask, normal pressure sterilizing, cooling, inoculating with strain, adding bran, stirring, placing into culture bag, and culturing.    USE - Method for cultivating mushroom (claimed).    ADVANTAGE - The method uses pure sawdust as culture medium, reduces pollution rate, saves production cost, and improves mushroom yield and quality.
NOVELTY - A vermiculture sludge treating method involves mixing sludge and agricultural waste and carrying out pre-processing fermentation. The pre-processed fermented mixture is cooled and added to a vermiculture bed as earthworm farming foodstuff. pH , temperature and humidity of the vermiculture bed are controlled. The earthworm food is digested. The sludge is converted to earthworm manure to obtain double products. The vermiculture bed is surrounded by an impermeable wall enclosed with a cover.    USE - Method for treating vermiculture sludge.    ADVANTAGE - The method enables treating vermiculture sludge without pollution and with enhanced earthworms vitality and increased sludge treatment.    DETAILED DESCRIPTION - A vermiculture sludge treating method involves mixing sludge and agricultural waste and carrying out pre-processing fermentation. The pre-processed fermented mixture is cooled and added to vermiculture bed, as earthworm farming foodstuff. pH, temperature and humidity of the vermiculture bed are controlled. The earthworm food is digested. The sludge is converted to earthworm manure to obtain double products. The vermiculture bed is surrounded by impermeable wall enclosed with a cover. Bottom and upper surfaces of wall are provided with vertical structure including adjustment layer and farmed layer. Bottom parts of a perforated drain pipe and perforated fabric tube are provided with the adjustment layer. An outside of the perforated drain pipe and a collection tank wall are connected through a perforation cloth tube. Geotextiles are provided between the adjustment layer and farmed layer. A surface of the farmed layer is provided with straw curtain, Ginkgo biloba, and dregs. The wall is provided with a wall pipe head.
NOVELTY - Obtaining Chinese magnolia vine fruit extract involves soaking Chinese magnolia vine fruit in 70% of aqueous acetone solution, and then extracting to obtain extraction liquid. Extraction liquid is filtered to obtain filter liquor. Filter liquor is extracted by utilizing ethyl acetate to obtain extract product. The extract product is eluted four times in a column chromatography containing silicon glue by utilizing chloroform and acetone in ratio of 10:1, 9:1 and 2:1, and then in chloroform and methyl alcohol ratio of 1:1 to obtain elution product.    USE - Method for obtaining Chinese magnolia vine fruit extract used as antibacterial for preparing antibacterial products (all claimed).    ADVANTAGE - The method enables to obtain Chinese magnolia vine fruit extract in eco-friendly manner.
NOVELTY - Eco-friendly biological pesticide comprises 15-26 pts. wt. berberine hydrochloride, 65-74 pts. wt. antimicrobial peptide of earthworm, 20-31 pts. wt. fennel oil, 1-3 pts. wt. matrine, 5-9 pts. wt. geranium oil, 3.5-6.4 pts. wt. trimeric sodium phosphate, 20-40 pts. wt. polyvinyl alcohol, 3-13 pts. wt. wheat straw powder, 5-7 pts. wt. clove, 15-20 pts. wt. ethylene acrylic acid copolyme, 5-9 pts. wt. paraquat, 3-9 pts. wt. celangulin and 88-97 pts. wt. water.    USE - Eco-friendly biological pesticide used in organic agricultural products.    ADVANTAGE - The eco-friendly biological pesticide is prepared in a simple manner, and has no toxicity.
NOVELTY - A cultured recombinant amniotic epithelial film remotely delivering method involves preparing a cylindrical gelatin sponge bottom pad and a gelatin sponge cylindrical ring containing a film sleeve. The bottom pad and the cylindrical ring are sterilized and placed into a culture hole. Recombination amniotic epithelial film is sleeved into inside of the cylindrical ring. The film is soaked in cell culture base and cell patch-filled gelatin sponges, followed by sealing film and performing remote delivery process.    USE - Method for remotely delivering cultured recombinant amniotic epithelial film.    ADVANTAGE - The method enables utilizing gelatin sponge as a three-dimensional bracket, so that culture sleeve can be firmly fixed. The method enables ensuring better trophic action on cells due to adsorption of nutrient solution, maintaining cell activity, avoiding pollution caused by leakage of the nutrient solution and realizing convenient remote delivery process.
NOVELTY - Separating methane from low-concentration methane gas, involves compressing and purifying low-concentration methane gas, subjecting the purified product to primary pressure swing adsorption and then deoxygenating, and subjecting the deoxygenated product to secondary pressure swing adsorption in the presence of nitrogen and then subjecting to tertiary pressure swing adsorption.    USE - The method is useful for separating methane from low-concentration methane gas (claimed).    ADVANTAGE - The method is capable of separating methane from low-concentration methane gas with improved separation efficiency and methane recovery rate of 85-90%.
NOVELTY - Preparation of polyamino silicon-coated magnetic nanoparticles involves preparing magnetic nanoparticles, preparing reverse microemulsion, adding magnetic nanoparticles to reverse microemulsion, adding tetraethyl orthosilicate and 3-aminopropyltriethoxysilane, hydrolyzing resulting mixture in presence of ammonia catalyst, forming surface-coated silicon layer on network-shaped structure, and loading polyamino groups on the surface of mesh structure.    USE - Preparation of polyamino silicon-coated magnetic nanoparticles useful in specific or non-specific isolation of DNA used for performing heterosexual hybridization (all claimed).    ADVANTAGE - The method improves isolation rate of DNA, provides nontoxic polyamino silicon-coated magnetic nanoparticles within a short period of time, by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for non-specific adsorption of DNA from target organism, which involves preparing to-be-detected DNA-containing buffer system, adding polyamino silicon-coated magnetic nanoparticles to buffer system, mixing, adding skim milk powder solution, and performing magnetic separation; and    (2) method for performing heterosexual hybridization of isolated target DNA sequence.
NOVELTY - A carbide slag is dried, crushed, sieved to particle size of 25-1700 mu m and pretreated. The pretreated carbide slag is added to acid solution, and acid-treated, to obtain metal salt mixed liquid. The pH of metal salt mixed liquid is adjusted to 10-13 using alkaline agent, to obtain solid precipitate. The solid precipitate is aged, filtered, washed, dried, calcined and activated, to obtain carbide slag-based solid alkali catalyst.    USE - Preparation of carbide slag-based solid alkali catalyst used for preparing biodiesel (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of carbide slag-based solid alkali catalyst, by simple method. The biodiesel with fatty-acid-alkyl-ester yield of 85% or more is formed using carbide slag-based solid alkali catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of carbide slag-based solid alkali catalyst for preparing biodiesel.
NOVELTY - A tissue-cultured Ulmus pumila rejuvenation method involves selecting single plant of tissue-cultured Ulmus pumila, transferring into subculture medium, allowing the seedling to grow to a height of 2.5-3.5 cm, cutting base callus tissue and blade base to obtain Ulmus pumila seedlings. The Ulmus pumila seedlings are transferred to a plant tissue culture rejuvenation medium, subjected with alternating light and dark culture, illuminated with light and cultured in dark at 19-23 degrees C for 40 days to give Ulmus pumila complex seedlings.    USE - Method for rejuvenation of tissue-cultured Ulmus pumila.    ADVANTAGE - The method enables rejuvenation of tissue-cultured Ulmus pumila with improved industrial production process, in eco-friendly manner.    DETAILED DESCRIPTION - A tissue-cultured Ulmus pumila rejuvenation method involves selecting single plant of tissue-cultured Ulmus pumila, transferring into the subculture medium for 21-25 days, allowing the seedling to grow to a height of 2.5-3.5 cm having 30-40% woody stems, cutting base callus tissue and blade base, retaining the top bud to a height of 1.8-2 cm to obtain Ulmus pumila seedlings. The Ulmus pumila seedlings are transferred to a plant tissue culture rejuvenation medium, subjected with alternating light and dark culture, illuminated with light at 23-27 degrees C for 13 hours with a light intensity of 1500-3500 LUX, cultured in dark at 19-23 degrees C for 40 days to give Ulmus pumila complex seedlings.
NOVELTY - Synthesis of liquefied natural gas comprises taking coke oven gas as raw material, preparing syngas, transferring to methanol synthesis unit, transferring to methane synthesis units and transferring to deep freezing unit.    USE - Method for synthesizing liquefied natural gas (claimed).    ADVANTAGE - The method is simple and has higher purity.
NOVELTY - This utility new type claims a energy-saving environment-friendly ecological circulation of a sewage treatment system, comprising excrement pool, a sewage of dejection and sewage pool inner inner sewage pool, marsh gas pool, marsh gas storage tank, storage tank, storage tank and biogas residue organic fertilizer storage tank, the excrement pool and sewage pool through pipeline is connected marsh gas pool, pool to carry out Anaerobic fermentation inner in marsh gas pool, a marsh gas and biogas liquid and biogas residue, marsh gas of the marsh gas pool through inner pipeline is sent to a biogas inner marsh gas storage tank, a marsh gas pool through pump A conveying to a biogas residue inner biogas storage tank, a marsh gas pool through pump B delivery to biogas residue storage tank, part inner the biogas liquid storage tank through a backflow pipe reflowing to marsh gas pool, a biogas storage tank and biogas residue storage tank through pipeline are connected organic fertilizer storage tank, this sewage processing system, through reasonable use of sewage for not only protecting the environment, and realize the resource of dung dirt use.
NOVELTY - This utility model claims a novel drying slag field, comprising field, discharging pipe and reflux pipe, periphery of the field body periphery provided with anchor; the field body top set with solar shed; the anchorage ditch side provided with return sand well, a return pipe A is connected to upper part of field body at another end a return sand well connecting to marsh gas pool, a return pipe and a marsh gas interface of the reflux pipe and field body interface level is below the horizontal plane, the slag drying field through reflux pipe, drying of a biogas reflux to a methane slag field in continuous fermentation, which prevents the loss of biogas slurry and increase the utilization rate of raw material.
NOVELTY - This utility new type claims a dust collection and a producing biomass granule fuel, comprising: a hollow shell, the a vertical set along the axial line, the lower housing end and a large diameter end a dust hopper, pulse bag-type dust collector, the lower end and the upper end connecting housing, a pulse bag dust collector at one side has set an air outlet, said air outlet comprises a ventilation pipe and air outlet cover,, a star-shaped discharger through the dust hopper and small calibre end connected, and each a electric connection and a control system. This utility new type is determined for wood dust bran unified collection, then processing into a biomass fuel particle, machine integrated design, which solves a factory dust problem, improves the working environment, at the same time solves the problem that the dust and use, direct a biomass fuel for boiler fuel, solves the problem that the artificial , and dust pollute large furniture factory, and it can increase use waste, the biomass fuel is a more high use value.
NOVELTY - A wet product mix of bromadiolone is distillation-dehydrated with organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation-dehydrated in film evaporator, wet-ground, modulated and packaged. Solution containing mancozeb, zinc complex and organic solvent is added to resulting mixture, and dehydration-crystal transformed, to obtain bromadiolone.    USE - Preparation of bromadiolone (claimed).
NOVELTY - Processing phenazine oxide comprises (i) mixing an organic solvent used in preparing phenazine oxide and phenazine oxide wet product, distilling and dehydrating; (ii) heating or heating, distilling and dehydrating through a film evaporator, wet grinding, modulating and packaging; and (iii) complexing in mancozeb and zinc containing organic solvent, dehydrating and carrying out crystal transformation.    USE - The method is useful for processing phenazine oxide (claimed).    ADVANTAGE - The method reduces decomposing of product, avoids fire accident in drying process and reduces generation of harmful impurities and dust.
NOVELTY - Preparing amitraz, comprises (i) mixing an organic solvent with amitraz wet product, distilling, and dehydrating; (ii) injecting solvent as a carrier while heating, or passing through a film evaporator, heating, distilling, and dehydrating dehydration, and carrying out wet grinding, modulating, and continuously packaging; and (iii) dehydrating mancozeb and zinc added with organic solvent, and simultaneously carrying out crystal transformation, to obtain the product.    USE - The method is useful for preparing amitraz (claimed).    ADVANTAGE - The method reduces the decomposition of product, and pollution caused by harmful impurities and dusts particles; and prevents the occurrence of fire accident while drying the product.
NOVELTY - A wet product mix of toxaphene is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation-dehydrated in film evaporator, dehydrated, wet-ground, modulated, and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain toxaphene.    USE - Preparation of toxaphene (claimed).    ADVANTAGE - The method enables preparation of toxaphene, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparing abamectin diesel oil comprises: (a) adding an organic solvent into distilled-dehydrated abamectin diesel oil wet product; (b) carrying out distillation and dehydration via injection heating or film evaporator, carrying out wet grinding, modulating and packaging for continuous operation; and (c) adding mancozeb and zinc organic solvent complex and dehydrating to crystallize.    USE - The method is useful for preparing abamectin diesel oil (claimed).    ADVANTAGE - The method avoids the pollution of harmful impurities and dust.
NOVELTY - Preparing salithion comprises (i) mixing salithion wet product and organic solvent, distilling and dehydrating, (ii) jet heating or through film evaporator heating, distilling and dehydrating, enabling dehydration process and wet smashing, modulating, carrying out package process continuous operation, and (iii) complexing mancozeb and zinc, dehydrating and carrying out crystal transformation process in organic solvent.    USE - The method is useful for preparing salithion (claimed).    ADVANTAGE - The method reduces harmful impurities and dust pollution, and avoids the occurrence of product drying process fire accident.
NOVELTY - A wet product mix containing lime sulfur is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain lime sulfur.    USE - Preparation of lime sulfur (claimed).    ADVANTAGE - The method enables preparation of lime sulfur, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Composting sludge involves utilizing air flotation pool (1), sludge adjusting pool (2), filter press feeding pump (3), high pressure volume sludge (4), belt conveyor (5), mud cake crushing device (6), transport device (7) and aerobic fermentation compost chamber (8).    USE - Method for composting sludge (claimed).    ADVANTAGE - The method enables to compost sludge economically by requiring less space.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a sludge composting method.    Air flotation pool (1)    Sludge adjusting pool (2)    Filter press feeding pump (3)    High pressure volume sludge (4)    Belt conveyor (5)    Mud cake crushing device (6)    Transport device (7)    Aerobic fermentation compost chamber (8)
NOVELTY - Biomass pyrolysis system comprises a feeder, a fluidization bed (1), a cyclone separator (2), a pre-heating furnace (3) and a gas buffer tank (4) that is connected to the pre-heating furnace, where a condenser (5) is installed with the cyclone separator. A filter (6) is connected to the condenser. A compressor (7) is connected to the filter.    USE - Biomass pyrolysis system.    ADVANTAGE - The biomass pyrolysis system enables to perform pyrolysis of biomass in an easy, quick and efficient manner at industrial scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass pyrolysis system.    Fluidization bed (1)    Cyclone separator (2)    Pre-heating furnace (3)    Gas buffer tank (4)    Condenser (5)    Filter (6)    Compressor (7)
NOVELTY - Raw material chosen from crop straw, rice husks, reed bamboo, broken branches and shrubs is crushed and pyrolyzed in a furnace at 260-340 degrees C to obtain low carbon powder. The low carbon powder is pulverized to 20-100 mesh using ball mill and mixed with preset amount of biomass tar to obtain a paste. The paste is extruded from an extruder into various shapes of charcoal. The charcoal obtained is pyrolyzed at 700-1000 degrees C and cooled to produce charcoal.    USE - Production of charcoal (Claimed).    ADVANTAGE - The method enables efficient production of charcoal having high calorific value and high density, economically and by a quick process.
NOVELTY - A wooden stick mechanism is manufactured by smashing crop straw, rice hull, Arundo donax, and shrub residual branch into pulverizer, drying at 200-300 degrees C, extruding into molding machine, and cooling at less than or equal to 180 degrees C in which dried raw material has moisture content of less than or equal to 10%.    USE - Manufacture of wooden stick mechanism (claimed).    ADVANTAGE - Process saves cost, and product has high calorific value and density.
NOVELTY - A non-cylindrical hollow mechanism wooden stick is prepared by selecting crop straw, rice husk, Arundo donax, and all kinds of miscellaneous shrub residual branches as raw materials, crushing, drying, and pressing in which wooden stick has hollow shape.    USE - Preparation of non-cylindrical hollow mechanism wooden stick (claimed).    ADVANTAGE - Product has large air contact area, fast and sufficient combustion, and uniform thickness and is energy-saving, environment-friendly, and convenient to transport.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a non-cylindrical hollow mechanism wooden stick.
NOVELTY - Plastic-type small and medium sized livestock and poultry farms software anaerobic device comprises an anaerobic tank, a feeding pipe, a discharge pipe, a pumping slag tube, an air guide pipe, and overflow pipe, a hook and perforated porous rib.    USE - The device is useful in the production of biogas.    ADVANTAGE - The device reduces the farm construction cost; and has easy utilization, and handling rate, high gas production rate, and simple installation effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the plastic-type small and medium sized livestock and poultry farms software anaerobic device.
NOVELTY - This utility new type provide the A a biomass granule breaking material machine, comprising gear and cutting material, below the gear set with multi-group uniform screw thread mounting hole, the screw thread mounting hole provided with a multi-matching using a bolt, a material cutting knife corresponding to multi-group screw thread mounting hole set with mounting disk, a material cutting knife through a bolt mounting disk fixed b the following gear. This utility new type change through a method of cutting tool material and material of cutting knife of traditional biomass material granule machine, can avoid abrasion of working panel, and cutting a ring mould material cutting knife and gear is bolt fixed connection is easy to change, this utility new type can effectively solve the problem of the existing technology change interrupt material cutter, this utility new type has simple structure, convenient and practical use is worth to be popularized.
NOVELTY - This utility new type provide the one upper rotational flow without a power circulation Anaerobic reactor, comprising tank body, centre a shunt, this shunt a center set has more of a shunt water outlet, the more of the middle water wherein each of a downstream are set has a guide flow plate, one of a waste water enter a water inlet to the tank body inner pipe, a water inlet pipe on the bottom of the tank body and a tank body side surface extending enter into to the center a inner flow, mixing liquid collection lifting device, lifting a collection in mixed liquid of a three phase separator, arrangement of mixing liquid separator in a three phase separator, set in the water pipe of the tank body upper part. Mixing liquid collection lifting device through mixed liquid lifting pipe connecting to mixing liquid separator, a three phase separator through biogas raising pipe connected to mixing liquid separator, between rear side position to the tank body outer side of the flow guide plate has connection for discharging sludge is sludge discharging pipe.
NOVELTY - This utility new type claims a planting farm waste comprehensive processing system, this system comprises dejection collection system, solid-liquid separating device, dung stirring mixing device, organic fertilizer output device, liquid manure regulating pool, marsh gas pool, slag recovery device, said dejection collection system solid-liquid separating device and a solid-liquid separating device respectively and a stirring mixing device and liquid dung excrement regulating pool, stirring dung and organic fertilizer output..., liquid manure regulating pool, marsh gas pool, slag recovery device are orderly connected, a biogas residue and a stirring mixing dung... This utility new type of farm excrement comprehensive processing system for farm excrement solid-liquid separating respectively carrying out process, making into organic fertilizer and used for a marsh gas, realize the feces multistage efficient use, reduce the farm manure for surrounding environment of influence.
NOVELTY - A A with organic waste and activated coke a deserted soil improvement agent degradation of device, comprising: pre-processing device, a conveying device, dry device, a vapour purification separating device, oil water separating device, sewage processing device, an oil storage device, cooling device, mixing device, a dust removing device, gas high temperature a solution pipe, waste heat recovery device, used for pre-processing organic waste is pre-processing device through the feeding end of conveying device and distillation device a, gas of dry distillation device from outside fuel pneuma, generating a mixed gas of a gas purification separating device separating, separating out of a gas back to a a dry distillation device, gas purification separating device is a oil water separating device, another end a spray water, oil water separating device separating the water delivery to a sewage treatment device, the separating of the second biomass oil conveying to storage device, the utility model is new type finish the organic waste and resource use of active coke powder, protect environment and promote virtuous economic circulation.
NOVELTY - This new utility model claims of a kind of household garbage one multi-layer rotary dry distillation device, by multi-layer feedstock system (1), a multi-layer rotary dry distillation device (2), a gas collection and purification system use (3), carbon discharging system (4), machine frame (5), a remote control system (6) is composed of, wherein the device wherein the multi-layer feedstock system (1) is output port and multi-layer rotary dry distillation device and feedstock port connected with the multi-layer rotary dry distillation device (2) and discharging port and carbon discharging system (4) input port is connected with the multi-layer rotary dry distillation device (2) and the air outlet and gas collection and purification using system (3) input end is connected with the multi-layer feedstock system (1), a multi-layer rotary dry distillation device (2), a gas collection and purification system use (3), carbon discharging system (4) installed on machine frame (5) above, a remote control system (6) and multiple layer system feedstock (1), multi-layer rotary dry distillation device (2), a gas collection and purification system use (3), carbon discharging system (4) , frame (5), remote control wireless connection.
NOVELTY - This utility new type claims a aerobic one. Anaerobic reaction are combined and a circulation type garbage processing system, comprising an aerobic biological leaching filter l, nozzle, Anaerobic reactor, a storage tank, a dewatering machine, a waste gas absorber, air blower and circulation pump, a spray head set in the aerobic biological filter l inner spraying nozzle through circulation pump and Anaerobic reactor connected, the air inlet of the air outlet and waste pneuma absorber upper part of said aerobic biological leaching filter l provided with feeding and an air outlet, wherein the aerobic biological leaching filter l lower part provided with a material wherein a liquid outlet, an aerobic biological leaching filter l is connected, wherein a material feeding and wherein dehydration machine connected, wherein the liquid inlet of the liquid outlet and wherein Anaerobic reactor connected, Anaerobic reactor provided with discharge wherein a liquid outlet, wherein the air inlet and discharge Anaerobic reactor of methane tank is connected. This utility new type using a structure can finish for a use of domestic garbage, and a relative short period, is large, a garbage can is thoroughly decomposing, is also very convenient.
NOVELTY - The ecological breeding method involves digging a pit in piggery ground, filling the pit with indigenous microorganism ferment pad material, and forming indigenous microorganism fermenting bed. The indigenous microorganism ferment pad material contains 2 kilograms per cubic meter of indigenous microorganism fermentation liquid of the total volume of 85-90 percent of organic padding, total volume of 10-15 percent of soil, and mixture of total weight of 55-65 percent of water and 0.3-0.5 percent of salt.    USE - Ecological breeding method for pigs.    ADVANTAGE - Reduces pollution of the environment since pig manure does not pollute the environment, does not affect the quality of water, has no odor, and does not cause mosquito breeding. Improves feed efficiency since pig manure is converted to inorganic salt necessary for the growth of pigs due to addition of indigenous microorganisms in organic litter. Ensures saving water and labor and improves efficiency in breeding pigs by reducing labor costs and improving work efficiency.
NOVELTY - The method involves adding Lupinus albus seeds into water. The water has volume of 5 units. The mixture is left to stand for 1 to 2 hours at 60 to 70 degrees Celsius. The seeds decompose by thermal process to free sparteine and anagyrine alkaloids into the water.    USE - Method for obtaining sparteine and anagyrine alkaloids from Lupinus albus plant, so as to produce a drug (claimed) for improved biological control against flies, mosquitoes, plant pests, agricultural insects, ticks, lice, bacteria, and all other kinds of insects and pests, as well as nematodes such as round worms. Can be used in agricultural applications, such as in greenhouses for fruits and vegetables.    ADVANTAGE - The drug or herbal medicine provides improved control against insects and pests or nematodes so as to completely eliminate these in fast, efficient manner without harming environment and human health.
NOVELTY - Biodiesel of higher fatty acids comprises at least 25-35 vol.% glycerol compounds and/or 36-45% of at least inedible mixtures, processed animal fats and oils, vegetable oils and at least 5-10% of esters of carboxylic acids, at least 5-10% of fusel oil, and 0.001-0.002% of a mixture of potassium hydroxide and sulfonic acid as an activator. In the biodiesel preparation, the activator which is a mixture of potassium hydroxide and sodium hydroxide with sulfonic acid is added in the mixing process in a mixer at a speed exceeding 3000 rpm.    USE - Used as biodiesel.    DETAILED DESCRIPTION - Biodiesel of higher fatty acids comprises at least 25-35 vol.% glycerol compounds and/or 36-45% of at least inedible mixtures, processed animal fats and oils, vegetable oils and at least 5-10% of esters of carboxylic acids, at least 5-10% of fusel oil, and 0.001-0.002% of a mixture of potassium hydroxide and sulfonic acid as an activator. In the biodiesel preparation, the activator which is a mixture of potassium hydroxide and sodium hydroxide with sulfonic acid is added in the mixing process in a mixer at a speed exceeding 3000 rpm, preferably the activator is a composition mixture obtained by combining 0.0015% of potassium hydroxide and 0.00002% sulfonic acid.
NOVELTY - Method for preparing extract, involves (a) adding 5-15 parts volume alcohol, ketone or ester solvent to 0.5-1.5 pts. wt. Alpinia officinarum, extracting obtained mixture, and decompressing and recovering solvent to obtain extract, (b) dissolving extract obtained in step (a) in water, and passing obtained solution through macroporous adsorption resin column, (c) performing primary elution using solvent, and (d) performing secondary elution using solvent, collecting eluate, recovering solvent, and decompressing and drying the eluate.    USE - The method is useful for preparing extract which is used in medicine for providing anticancer effect with respect to liver cancer and gastric cancer (all claimed).    DETAILED DESCRIPTION - Method for preparing extract, involves (a) adding 5-15 parts volume alcohol, ketone or ester solvent to 0.5-1.5 pts. wt. Alpinia officinarum, extracting obtained mixture for 2-4 times for 1-3 hours (each time), and decompressing and recovering solvent to obtain extract, (b) dissolving extract obtained in step (a) in water, and passing 6-10 volumes of obtained solution through macroporous adsorption resin column at a flow rate of 1-3 BV/hour, where the weight-volume ratio of extract and water is 1:2.5-10, the column diameter-height of resin is 1:4-13, and the resin is eluted using 1-5 times water at a flow rate of 2-6 BV/hour, (c) performing primary elution using 5-8 times solvent having concentration of 30-50 vol.% at a flow rate of 4-9 BV/hour, where the solvent is methanol, ethanol or acetone, and (d) performing secondary elution using 5-8 times solvent at a flow rate of 4-9 BV/hour, collecting eluate, recovering solvent, and decompressing and drying the eluate, where the solvent is 80-95 vol.% methanol, ethanol or acetone.
NOVELTY - A natural iron ore-supported nickel catalyst comprises a carrier, pre-calcined iron-containing natural ore granules, nickel oxide and iron in a ratio of 0.03:1-20:1. The loading amount of catalyst is 2-15%.    USE - Natural iron ore-supported nickel catalyst is used for carbon dioxide/carbon monoxide methanation of coal-based and biomass-based syngas in slurry bed and moving bed.    ADVANTAGE - The environmentally-friendly natural iron ore-supported nickel catalyst can be prepared by a simple, economical and easy method with high catalytic activity, strength, wear resistance, and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the nickel based catalyst, which involves crushing iron-containing natural ore into granules having a diameter of 0.05-8 mm at 500-130 degrees C for 1-5 hours, cooling the granules to room temperature to obtain a particulate, adding 0.1-8 mol/l aqueous solution of nickel salt, carrier and iron to the particulate, uniformly mixing, impregnating the mixture and then absorbing, sintering the mixture and then drying, and baking.
NOVELTY - Fertilizer is prepared using urea, ammonium bicarbonate, potassium chloride, Bacillus licheniformis, B.subtilis, nystatin, proline, methionine, glycine, threonine, tyrosine, ferrous sulfate, manganese sulfate, zinc sulfate, calcium superphosphate, sodium humate, borax, medical stone powder, thiourea, diatomaceous earth, phosphate, peanut cake, corn straw, sugar residue, rapeseed cake, tobacco residue, wheat bran, nicotine, traditional Chinese medicinal residue, radix ilicis pubescentis, and radix sophorae flavescentis.    USE - As fertilizer for peanut.    DETAILED DESCRIPTION - Fertilizer is prepared using 20-30 pts. wt. urea, 30-40 pts. wt. ammonium bicarbonate, 15-20 pts. wt. potassium chloride, 2-3 pts. wt. Bacillus licheniformis, 1-2 pts. wt. B.subtilis, 2-4 pts. wt. nystatin, 20-25 pts. wt. proline, 18-23 pts. wt. methionine, 15-20 pts. wt. glycine, 20-25 pts. wt. threonine, 16-20 pts. wt. tyrosine, 20-25 pts. wt. ferrous sulfate, 15-18 pts. wt. manganese sulfate, 13-17 pts. wt. zinc sulfate, 15-20 pts. wt. calcium superphosphate, 20-30 pts. wt. sodium humate, 18-23 pts. wt. borax, 15-20 pts. wt. medical stone powder, 18-20 pts. wt. thiourea, 15-20 pts. wt. diatomaceous earth, 15-23 pts. wt. phosphate, 40-50 pts. wt. peanut cake, 50-60 pts. wt. corn straw, 20-30 pts. wt. sugar residue, 15-20 pts. wt. rapeseed cake, 5-10 pts. wt. tobacco residue, 20-40 pts. wt. wheat bran, 5-10 pts. wt. nicotine, 1-3 pts. wt. traditional Chinese medicinal residue, 10-13 pts. wt. radix ilicis pubescentis, and 12-15 pts. wt. radix sophorae flavescentis.
NOVELTY - The structure has a furnace shell (1) whose two ends are respectively provided with a front opening and a rear opening. The rear opening is equipped with a rear close cover (2). A steam discharge pipe (4) and a water discharge pipe (5) are respectively connected with an external steam source and an external water source. A lower part of a steam level section (42) is opened with a steam discharge port. The steam discharge pipe is arranged far away from a front end of the furnace shell. A top end of the furnace shell is connected with a steam rising section (43).    USE - Wood charring furnace structure.    ADVANTAGE - The structure has high carbonization efficiency, and is energy-saving and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a wood charring furnace structure.    Furnace shell (1)    Rear close cover (2)    Steam discharge pipe (4)    Water discharge pipe (5)    Steam level section (42)    Steam rising section (43)
NOVELTY - The device has an air inlet pipe connected with a smoke tube and another air inlet pipe. The air inlet pipes are extended into a purification pool. An end of air outlet pipe is connected with the latter air inlet pipe. Another end of the air outlet pipe is connected with a pneumatic pump. The purification pool is provided with an opening and closing drain pipe. The air outlet pipe is connected to bottom of a biomass boiler.    USE - Biomass boiler smoke dust purification device.    ADVANTAGE - The device is simple in structure, inexpensive and convenient to use and operate. The device has high smoke dust purification efficiency and energy-saving effect, and increases heat efficiency of the biomass boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biomass boiler smoke dust purification device.
NOVELTY - Biological carbonaceous briquette comprises carbon powder mixture obtained by carbonizing cotton stalk and wood chips, fuel additive, adhesive, oil, combustion improver and desulfurization agent. The amount of oil is 0.1-5%, combustion improver is 0.3-0.8% and desulfurization agent is less than 2%.    USE - Used as biological carbonaceous briquette.    ADVANTAGE - The briquette has high comprehensive combustion index and low ignition point, and is suitable for long distance transport.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing biological carbonaceous briquette, comprising (i) crushing cotton stalk and wood chips into granularity of less than 1 mm and drying in a drying tank to moisture content of less than 10%, (ii) mixing cotton stalk and wood chips of weight ratio 1:1-3:1 and carbonizing in a muffle furnace at 500-600 degrees C for 30 minutes at the heating speed of 10 degrees C /minute to obtain carbon powder mixture, (iii) mixing carbon powder mixture and adhesive, adding 0.3-0.8% combustion improver, and mixing to obtain mixture, (iv) adding the mixture into a carbon molding machine and molding into carbon block, and (v) drying and curing to moisture content of 2-5%.
NOVELTY - The cellar has a feeding tube comprising a feeding entrance and a material exit. A discharging pipe is connected with a material entrance and a discharging exit. A feeding outlet is connected with a discharging door. A cellar cover is connected with a seal rubber ring. A seal rubber is connected with an inner end and an outer end. An inner end of the seal rubber ring is connected with end face periphery of a main body part. The seal rubber ring is connected with an inner wall of a kiln body. An outside terminal and inner terminal are connected with a water tank.    USE - Water pressure seal biogas pneuma cellar.    ADVANTAGE - The cellar is convenient to use, safe and reliable, and increases methane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water pressure seal biogas pneuma cellar.
NOVELTY - Straw decomposition agent comprises Bacillus subtilis, Bacillus licheniformis, Saccharomyces cerevisiae, Aspergillus niger and Trichoderma koningii.    USE - The straw decomposition agent is useful for decomposing cellulose, hemicellulose and lignin.    ADVANTAGE - The straw decomposition agent comprising bacteria exhibits synergistic effect. The method increases the rate of decomposition on timely basis, where straw can be effectively degraded in 15 days; has simple, and easy preparation procedures; performs culturing process under room temperature conditions; and does not require the utilization of high cost culture agents, and thus it is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing straw decomposition agent, comprising culturing Bacillus subtilis, bacillus licheniformis, Saccharomyces cerevisiae, Aspergillus niger and Trichoderma koningii, where the cultured bacterial concentration is 0.1-1x 108/ml, uniformly mixing the number of bacteria, inoculating the bacteria into sugarcane leaves for 5-10 days in a ratio of 1:10-20, and culturing at 25-30 degrees C, until the moisture content in sugarcane leaves reaches 30-50%, and crushing the sugarcane leaves to 20-100 mesh, to obtain the final product.
NOVELTY - A Streptomyces hygroscopicus strain B04 (CGMCC 9918), is new.    USE - The S.hygroscopicus strain B04 is useful for preparing biocontrol agent for preventing and controlling black root disease of strawberry root rot (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing biocontrol agent, which involves (a) inoculating the above-mentioned S.hygroscopicus strain B04 on fermentation medium comprising earthworm manure and wheat bran and (b) fermenting the inoculum to obtain product.
NOVELTY - A low-carbon fermentation gas synthesizing method involves mixing carbon dioxide with oxygen and compressing the mixture. The resultant precipitate is post-fermented and synthesized to obtain fermentation gas.    USE - Method for synthesizing low-carbon fermentation gas that is utilized as factor for gasifying coal, lignite, biomass, municipal or industrial waste containing coal, sludge digestate and sediment.
NOVELTY - Producing natural gas and hydrogen using coke oven gas, comprises (i) pre-processing coke furnace gas, and taking out sulfur, tar, benzene and naphthalene; (ii) mixing coke furnace gas and water vapor, and performing low temperature sulfur-tolerant conversion reaction, converting main portion of carbon-monoxide of coke furnace gas into hydrogen gas, and converting organic sulfur in coke oven gas into inorganic sulfur; (iii) separating pure hydrogen product, methane gas and crude desorption exhaust gas; and (iv) taking out acid gases and organic sulfur, to obtain the final product.    USE - The method is useful for producing natural gas and hydrogen using coke oven gas (claimed).    ADVANTAGE - The method has simple process, low energy consumption, and easy operation procedure; is economical; and produces large amount of hydrogen by-products, and thus it achieves efficient utilization rate of coke oven gas.    DETAILED DESCRIPTION - Producing natural gas and hydrogen using coke oven gas, comprises (i) pre-processing coke furnace gas by adding into a pre-processing system, and taking out sulfur completely, and taking out tar, benzene and naphthalene; (ii) mixing coke furnace gas and water vapor in a sulfur-tolerant conversion system, and carrying out low temperature sulfur-tolerant conversion reaction, converting main portion of carbon-monoxide of coke furnace gas into hydrogen gas, and simultaneously converting large portion of organic sulfur in coke oven gas into inorganic sulfur; (iii) passing the transformed coke oven gas through a pressure swing adsorption system or a membrane separation unit, and separating pure hydrogen product, methane gas and crude desorption exhaust gas; and (iv) passing the material from the pressure swing adsorption system into a crude methane gas purification system, and taking out acid gases and organic sulfur, to obtain the final product.
NOVELTY - Direct methanation of raw gas is performed by preheating (S100) raw gas, alternately carrying out methanation (S400) and conversion (S300) to obtain crude methane, and desulfurizing and decarburizing (S500) to obtain refined methane.    USE - Direct methanation of raw gas (claimed).    ADVANTAGE - The methanation is more reasonable, has low investment and shortened process, and saves energy consumption and configuration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for raw gas direct methanation system comprising gas preheater, pre-chemical reactor connected to preheater through preheating which obtains compound premix gas, hydrogen carbon regulator connected to pre-chemical reactor and is adapted to carry out conversion reaction, methanation reactor connected to hydrogen carbon regulator and is adapted to carry out multi-stage methanation and obtains crude methane and steam, and desulfurization/decarburization connected to methanation reactor and is adapted to carry out desulfurization and decarburization.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of direct methanation of raw gas. (Drawing includes non-English language text).    Preheating (S100)    Pre-formation (S200)    Conversion (S300)    Methanation (S400)    Desulfurization and decarburization (S500)
NOVELTY - A micronutrient fertilizer components preparing method involves utilizing biomass in form of microalgae, spirulina, seed berries and mushroom substrate. Carboxyl, hydroxyl or phosphoryl functional groups existed on a surface of cell walls of the biomass are bound with trace elements such as iron, 3.0-12 mg/g manganese, 5.0-35.0 mg/g zinc and 12-40 mg/g copper to obtain a finished product. The fertilizer is applied to soil before sowing, where the micronutrients are presented in edible parts of plants.    USE - Method for preparing micronutrient fertilizer components that is applied for food crops such as grains of maize, barley, wheat or rice.
NOVELTY - Method of cultivating grapes involves (a) pruning grape vines, (b) carrying out soil and fertilizer management measures by plowing cultivation soil, and applying 3000-4000 kg per acre organic fertilizer and 200-300 kg chicken manure, and (c) carrying out pest control measures by spraying low-toxicity pesticide residue and removing diseased leaves.    USE - The method is useful for cultivating grapes (claimed).    ADVANTAGE - The method enables to cultivate nutritious and environmentally-friendly grapes.
NOVELTY - Production of methane gas involves using activated sludge, and gas generating synergist as raw materials.    USE - Production of methane gas (claimed).    ADVANTAGE - The method provides methane gas by adjusting carbon-nitrogen ratio of gas generating synergist to 10-12, and adjusting pH to 7-7.5 using limewater, with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for generating methane gas, which consists of tank, and canister or container.
NOVELTY - Fertilizer comprises 32-34 pts. wt. pea straw stick, 27-29 pts. wt. peanut straw stick, 23-25 pts. wt. melon vine, 18-20 pts. wt. prepared duck manure, 16-18 pts. wt. burnt clay, 13-15 pts. wt. leaf mould, 12-14 pts. wt. ammonium chloride, 7-9 pts. wt. cuprous oxide, 3-5 pts. wt. Agrobacterium tumefaciens manure, 1-3 pts. wt. humic acid, 2-4 pts. wt. crop straw stick preparation, 1-3 pts. wt. ammonium molybdate, 3-5 pts. wt. forchlorfenuron and 50-60 pts. wt. water.    USE - Fertilizer used for pecan (claimed).    ADVANTAGE - The fertilizer promotes growth of pecan, pecan has improved fragrance, and sweet taste, improves soil quality, and prevents nutrient loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing pea straw stick, peanut straw stick, melon vine and prepared duck manure and crushing through 40 meshes to obtain a mixture;    (B) mixing remaining components with water to obtain a product;    (C) mixing the product with obtained mixture and then stirring for 20 minutes to obtain a product; and    (D) keeping the product for 0.5 hours to obtain final product.
NOVELTY - Preparing 4-aza-5-androsten-3-one-17 beta -carboxylic acid compounds (I) from hydrogenation mother liquor recycled materials, comprises (a) dissolving 4-aza-5 beta -androst-3-one-17 beta -carboxylic acid compounds (II) and 4-aza-5 alpha -androst-3-one-17 beta -carboxylic acid compounds (III) in glacial acetic acid, adding palladium/carbon catalyst, and carrying out dehydrogenation under oxygen pressure, (b) cooling obtained reaction product, separating, and removing palladium/carbon catalyst, and (c) concentrating the filtrate under reduced pressure, adding methanol, and carrying out freezing-crystallization.    USE - The method is useful for preparing 4-aza-5-androsten-3-one-17 beta -carboxylic acid compounds.    ADVANTAGE - The method: has simple process and low cost; utilizes easily available recycled raw materials; and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparing 4-aza-5-androsten-3-one-17 beta -carboxylic acid compounds of formula (I) from hydrogenation mother liquor recycled materials, comprises (a) dissolving 4-aza-5 beta -androst-3-one-17 beta -carboxylic acid compounds of formula (II) and 4-aza-5 alpha -androst-3-one-17 beta -carboxylic acid compounds of formula (III) (hydrogenation mother liquor recycled materials) in glacial acetic acid, adding palladium/carbon catalyst, heating and carrying out dehydrogenation reaction under oxygen pressure to obtain a reaction product, (b) cooling the reaction product, separating, and removing palladium/carbon catalyst, and (c) concentrating the filtrate under reduced pressure, adding methanol, and carrying out freezing-crystallization to obtain final product.    R = carbonyl, carboxylic acid, carboxylic acid ester, amide, acetyl, hydroxy, hydrocarbon, ether or chloro.
NOVELTY - Fertilizer comprises 27-29 parts mass nitrogen fertilizer, 22-24 parts mass phosphate fertilizer, 16-18 parts mass potash fertilizer, 17-19 parts mass clover green manure, 12-14 parts mass peanut fertilizer, 8-10 parts mass diammonium phosphate, 6-8 parts mass manure, 12-14 parts mass magnesium sulfate, 7-9 parts mass soil conditioning agent, 3-5 parts mass lime powder, 4-6 parts mass alginic acid, 1-3 parts mass boron and magnesium fertilizers, 3-5 parts mass stem strengthening agent and 50-70 parts mass water.    USE - The fertilizer is useful for Agastache (claimed).    ADVANTAGE - The fertilizer has reduced dosage and residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves mixing the above-mentioned raw materials, and drying mixture.
NOVELTY - A nickel catalyst comprises 0.1-50 wt.% nickel supported mesoporous alumina gel carrier containing phosphorus. The atomic ratio of carrier and aluminum is 0.01-1.    USE - Nickel catalyst is used in manufacture of hydrogen gas (claimed).    ADVANTAGE - The nickel catalyst enables efficient manufacture of hydrogen gas with high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of nickel catalyst, which involves dissolving aluminum precursor and phosphorus precursor in aqueous solvent, mixing, adding epoxide, condensing, aging the resultant wet gel at room temperature, heat-treating, obtaining heat-treated mesoporous alumina gel carrier, dipping nickel precursor solution in the obtained mesoporous alumina gel carrier, heat-treating and drying; and    (2) manufacture of hydrogen gas, which involves performing steam reforming reaction of liquefied natural gas with catalyst at 500-900 degrees C.
NOVELTY - A biological oil preparation method involves drying, crushing, sieving bagasse and water-tetra-hydro-naphthalene-mixed solvent in a reaction kettle, and stirring, liquefying under anaerobic condition and cooling. The liquid product from residue is separated by low-pressure suction filtration. The reaction kettle and filtered residue is washed followed by carrying out reduced pressure distillation on dichloromethane washing liquid and acetone washing liquid to evaporate solvent and water in the product.    USE - Method for preparing biological oil.    ADVANTAGE - The method enables increasing liquefaction efficiency of bagasse, and improving biological oil yield, and conversation rate reaches over 98%, and biological oil yield reaches over 40%.    DETAILED DESCRIPTION - A biological oil preparation method involves drying, crushing, sieving, drying bagasse and water-tetra-hydro-naphthalene-mixed solvent together in a reaction kettle, stirring at 200-320 degrees C and liquefying for 0.5-1.5 hours under anaerobic condition, cooling the reaction kettle body and releasing pressure of the reaction kettle body after the reaction is ended. The kettle is opened, solid and liquid products are taken out of the reaction kettle. The liquid product from residue is separated by low-pressure suction filtration. The reaction kettle and the filter residue is washed using dichloromethane and acetone followed by carrying out reduced pressure distillation on dichloromethane washing liquid and acetone washing liquid at 30-70 degrees C to evaporate solvent and water in the product.
NOVELTY - The present invention provides a manufacturing method of ethanol-containing biomass ethanol fermentation broth, which includes: preparing an ulva powder; adding the ulva powder into a strain liquid capable of producing agar enzyme marine strains, in order to induce a crude enzyme solution; for hydrolysis of the ulva powder under a thermal environment and acidic solution, obtain an ulva polysaccharide hydrolyzate; adding a cellulase, an amylase enzyme and the said crude enzyme solution into the ulva polysaccharide hydrolyzate, to obtain an ulva oligosaccharide hydrolyzate; and obtaining an ethanol-containing biomass ethanol fermentation broth through fermentation between ulva oligosaccharide water solution and yeast strains. The present invention, under thermal environment, acidic solution and crude enzyme solution, uses natural yeast to hydrolyze the ulva polysaccharide hydrolyzate and obtain an ulva oligosaccharide hydrolyzate, then perform a fermentation process to produce a biomass ethanol which has medicine or food applications.
NOVELTY - The present invention discloses a treating agent for deodorization and decomposition of sludges and organic wastes and a treating method. The treating agent is obtained by mixing an activated matrix and a liquid solution. The composition of the activated matrix at least contains rice bran, soybean powder, sugarcane bagasse powder, bitter tea powder, rice wine, vinegar, molasses, as well as a mixture of at least four trace minerals of iron, aluminum, magnesium, and silicon; the above components are mixed according to a specific proportion to form the activated matrix. The liquid solution is obtained by activating water with strains of bacteria consisting of at least lactic acid bacteria, yeast and Streptomyces lividans. By mixing the activated matrix and the liquid solution to become a water solution mixture, the treating agent is thus produced. When in use, the treating agent is added into water which is 20~300 times of the treating agent by volume and the resulting mixture is fully stirred to become a diluted treating agent, and then the diluted treating agent is fully sprayed on a heap of sludges or organic wastes to remove the odor of the sludges or the organic wastes and to decompose viscous substances in order to improve the dehydration rate.
NOVELTY - A recycling treatment system for industrial low-concentration organic waste water and effluent is sequentially disposed with: a pretreatment device, a B-PAC (bioactive carbon) device, a MMF (multi-layer filtration) device, a UF (ultra-filtration) device, and an RO (reverse oasis) device; and by adding a ferrous ion generating agent and/or an electric charge neutralizer, the microbial activity in the water is made to adequately react with organic substances to make polar substances inert and reduce adhesion of the polar substances towards the filtration film, enhancing the lifespan of the filtration film and obtaining recycled industrial water conforming to the safety regulation.
NOVELTY - The converter has a band (1) that is arranged with a set of electrochemical cells placed one behind the other according to a longitudinal axis (A) of the band. The cells are connected in series by a set of electric connection strips (3). A set of spacers (5a, 5b) is arranged for realization a hydrogen transport pipe that is utilized for transporting the hydrogen to a set of anodes. The spacers are arranged with a closing band (6) parallel to the former band. An anodic hydrogen diffuser (10) i.e. anodic grid, is placed between faces of the former band and the closing band.    USE - Electrochemical converter for use in a standard fuel cell.    ADVANTAGE - The spacers are arranged with the closing band parallel to the band, and the anodic hydrogen diffuser is placed between faces of the band and the closing band, thus ensuring better cooling of the converter, providing a greater facility of realization of the rolled up converter, better distribution of the hydrogen side anodes, filtering of the air on cathodes, and ensuring better water management with regard to anodes and cathodes. The converter is compact, robust and relatively light.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a segment of an electrochemical converter.    Longitudinal axis (A)    Band (1)    Electric connection strips (3)    Spacers (5a, 5b)    Closing band (6)    Anodic hydrogen diffuser (10)
NOVELTY - A visible-light-responsive composition comprises 20-50 mol% strontium, 30-50 mol% bismuth, and 20-40 mol% iron, and oxygen.    USE - Visible-light-responsive composition for photosensors, and photoelectrodes and photocatalysts used for hydrolysis (all claimed) to produce hydrogen. Can also be used for removing and deodorizing environmental pollutants, antimicrobial, antiviral, antifungal, antifogging and antifouling materials, and in buildings and motor vehicles.    ADVANTAGE - The visible-light-responsive composition exhibits excellent photoelectric current responsiveness with respect to visible light irradiation. The photocatalyst obtained using the composition has high surface area and crystallinity. Absorption-utilization of visible light is accelerated in photoelectrodes using the composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrolysis method using a photoelectrode and/or a photocatalyst comprising the visible-light-responsive composition.
NOVELTY - The electrolyzer (10) has unit cell (12) on which a separator is laminated, and an end plate (20a) arranged by lamination direction at ends of a cell unit (14) at which unit cells are stacked. A piston unit (70) that presses the cell unit in lamination direction is provided between one end plate and cell unit. An insulation unit (80) is provided between piston unit and end plate. An electrically insulating knock unit (82) whose length along axial direction is larger than thickness of insulation unit is arranged in a hydrogen communicating hole (38c) when the insulation unit is connected.    USE - Differential pressure type high-pressure water electrolyzer for electrolyzing water and generating oxygen and hydrogen for fuel cell.    ADVANTAGE - Since the electrically insulating knock unit is arranged in the hydrogen communicating hole, while the insulation unit is provided between the piston unit and the end plate, in contact with the insulation part, the knock unit is only set to the thickness which ensures the insulation distance of hydrogen communicating hole, and the thickness of the insulation unit is reduced, and size reduction of the whole apparatus is executed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the differential pressure type high-pressure water electrolyzer.    Differential pressure type high-pressure water electrolyzer (10)    Unit cell (12)    Cell unit (14)    End plate (20a)    Hydrogen communicating hole (38c)    Piston unit (70)    Insulation unit (80)    Electrically insulating knock unit (82)
NOVELTY - The plant has zones (24-28) that are arranged in a row (39,40) between the ends (2,4) of a container to be consecutively passed by the biologic material fed through the container. Each zone is comprised of the stirring elements (29-38). The stirring element of each zone is controlled separately from the stirring elements belonging to specific zones. A control unit is configured to control stirring, temperature and duration of stay of the organic material present in each zone separately for each zone by controlling stirring elements.    USE - Plant for biological degradation of organic material through dry fermentation for production of biogas.    ADVANTAGE - The blocking element is controlled through the control unit for influencing the speed by which the organic material is fed into the container. The angle is adjusted for the uppermost blade-like element of each stirring element, so as to be efficiently influenced to break the upper surface layer of the biomass to smoothly leave the biomass within which biogas is produced. The delimitation of adjacent zones results in a good possibility to control the duration of stay and the treatment of the organic material without any remarkable influence, and ensures that the material is fed with the desired speed from one zone to other zone without prolonged or shortened duration of stay in the zone of material coming into particular portion of zone with respect to other material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant for biological degradation of organic material through dry fermentation for production of biogas.    Ends of container (2,4)    Longitudinal side wall (19)    Zones (24-28)    Stirring elements (29-38)    Rows of stirring elements (39,40)
NOVELTY - The method involves directing gases from a power plant (12) to a first stage cooling unit (16). Combined gas and liquid solution from the first stage cooling unit is pumped to a first gas-liquid separator (24). The gases from the first gas-liquid separator are directed to a second stage cooling unit (18). The combined gas and liquid solution from the second stage cooling unit is pumped to a second gas-liquid separator (26). The cleaned gases from the second gas-liquid separator are directed on to be used for commercial applications.    USE - Method for cleaning-up emitted gases from various types of power plants such as plasma gasification plant and fossil fuel fired power plant (all claimed).    ADVANTAGE - The method enables separating impurities from exhaust gases emitted from the power plant using a temperature-based system. The method enables cleaning-up the exhaust gases in a simple, safe and cost effective manner for removing detrimental compounds/elements from the gases being emitted from the power plant.    DETAILED DESCRIPTION - The cleaned gases directed from the second gas-liquid separator are selected from one of carbon monoxide (CO), hydrogen (H2), methane (CH4) and inert nitrogen (N2).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for cleaning-up emitted gases from various types of power plants.    Power plant (12)    Cooling units (16, 18)    Gas-liquid separators (24, 26)    Downstream commercial application (30)    Temperature regulator (34)
NOVELTY - The method involves feeding further cooled and partially condensed gaseous feed to a first fractionation column (210), and separating into first bottom stream (220) having high carbon dioxide (CO2) concentration than gaseous feed, and first overhead stream (225) having high methane concentration than gaseous feed. A first overhead stream is fed to second fractionation column (255), and is separated into second bottom stream (260) having high CO2 concentration than first overhead stream, and second overhead stream (285) having high methane concentration than first overhead stream.    USE - Method for separating carbon dioxide from gaseous feed comprising methane and carbon dioxide, used in oil recovery process of oil field.    ADVANTAGE - The carbon dioxide is efficiently separated from gaseous feed while reducing the refrigeration requirement, and power consumption. The oil recovery process is performed efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for separating carbon dioxide from gaseous feed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the carbon dioxide separation process.    First fractionation column (210)    First bottom stream (220)    First overhead stream (225)    Second fractionation column (255)    Second bottom stream (260)    Second overhead stream (285)
NOVELTY - This utility new type provide the a urine collecting cup, a cover, a connecting rod, a through shaft and a column, a handle, a cup connected in turn. This utility new type has simple structure, convenient use, urine sample is not easy to pollute, urine is not easy to overflow, for a quadratic a small amount of urine collection, but also can collect a total a urine.
NOVELTY - Bottom disposable urine detection sample reserving l, l urea (1) is scave with ruler (8) is funnel, the lower part hopper is tightly connected transverse has a hollow cylinder (2), hollow cylinder (2) towards the connecting tube (6) is hollow head close to the urine l (1) connecting pipe of one end (6) is a transverse section is U-shaped of U-shaped small pipe (5), a U-shaped small pipe (5) towards the bottom urine l (1), U-shaped small pipe (5) has a bottom flow into hole (4) close to the small U-shaped pipe (5) lower part tube body of the edge outside a t a and a groove (3) matched with a (10), a U-shaped large tube (6) opening part of upper part with inner screw thread, (7) opening part is a part with a U-shaped large tube (6) inner screw thread is matched with the outside screw thread. This utility new type safe and reliable integrated can create a lock, convenient, sanitary, sealing, it is not easy to pollute hand and environment, can measure urine.
NOVELTY - Sustained aerobic biological filter chamber comprises water inlet (1), double-layer filter film (2), clapboards (3,9), bioreactor (4), filter bag (5), water outlet (6), manganese dioxide (7) and microcapsule (8).    USE - Sustained aerobic biological filter chamber.    ADVANTAGE - The sustained aerobic biological filter chamber is environmental-friendly and has simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sustained aerobic biological filter chamber.    Water inlet (1)    Double-layer filter film (2)    Clapboard (3,9)    Bioreactor (4)    Filter bag (5)    Water outlet (6)    Manganese dioxide (7)    Microcapsule (8)
NOVELTY - Method for promoting biodegradation of perfluorinated compounds in sewage residue involves (a) adjusting pH of the sewage residue to alkaline, (b) adding surfactant to the resulting residue in weight ratio of 0.05-0.50: 1 and (c) subjecting the resulting mixture to anaerobic fermentation to degrade perfluorinated compounds.    USE - The method is useful for promoting biodegradation of perfluorinated compounds in sewage residue. The perfluorinated compound is perfluorooctanoic acid (PFOA) and perfluorooctanesulfonic acid (PFOS) (all claimed).
NOVELTY - The device has a main portion that is provided with a pre-processing probe (11), a sludge fermentation tank (12) and a fermentation stirrer (13). A medicine box (20) is arranged at the bottom portion with a magnetic stirrer (16). The pre-processing probe is connected with a pre-processing sludge pump (7). A heating rod (18) is provided in the residual sludge tank (15). The medicine box is provided with a pre-processing sludge discharging pump (5) connected with an acid pump (19).    USE - Device for preprocessing strong alkali used for performing reinforcing surplus sludge alkaline fermentation for producing acetic acid.    ADVANTAGE - The alkaline fermentation is improved and the acetic acid production content is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preprocessing strong alkali.    Pre-processing sludge discharging pump (5)    Pre-processing sludge pump (7)    Pre-processing probe (11)    Sludge fermentation tank (12)    Fermentation stirrer (13)    Residual sludge tank (15)    Magnetic stirrer (16)    Heating rod (18)    Acid pump (19)    Medicine box (20)
NOVELTY - Photocatalyst comprises a conductive material having graphene nanostructures attached to the surface of a photoactive metal oxide semiconductor including strontium titanate or cerium oxide, where the photoactive metal oxide semiconductor has a microstructure or larger structure.    USE - The photocatalyst is useful for catalyzing photocatalytic electrolysis of water to convert water to hydrogen and oxygen (claimed).    ADVANTAGE - The photocatalyst: utilizes noble metals dispersed on the surface of a photoactive material; reduces or suppresses electron-hole recombination rate; decreases the complexity and costs associated with photocatalytic water-splitting systems.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a water splitting system comprising a transparent container comprising the photocatalyst as aforementioned, and a light source for irradiating the aqueous solution; and    (2) converting water to hydrogen and oxygen, comprising irradiating an aqueous solution comprising the photocatalyst and water with UV irradiation, where water is converted into hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the water splitting system.    Photocatalyst system (10)    Photoactive metal oxide (12)    Excited electron (13)    Conductive band (15)    Graphene nanostructure (17)
NOVELTY - A desulfurization system comprises desulfurization unit (3) containing sulfur, hydrodesulfurization catalyst precursor (P1) containing metal oxides chosen from nickel oxide, cobalt oxide, molybdenum oxide and tungsten oxide, and hydrogen-sulfide adsorption agent (A1) containing zinc oxide. The desulfurization system hydrodesulfurizes the fuel gas.    USE - Desulfurization system is used in hydrogen production system of fuel cell system (all claimed).    ADVANTAGE - The desulfurization system enables efficient desulfurization of fuel gas without pre-processing and re-reduction process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen production system, which comprises desulfurization system, and hydrogen-generating unit (4) which generates hydrogen from the fuel gas de-sulfurized in the desulfurization unit;    (2) desulfurization of fuel gas, which involves contacting hydrodesulfurization catalyst precursor (P1) and hydrogen-sulfide adsorption agent with hydrogen in the fuel gas, and sulfurating the hydrodesulfurization catalyst precursor (P1) and hydrodesulfurization catalyst; and    (3) manufacture of desulfurization catalyst, which involves contacting hydrodesulfurization catalyst precursor (P1) and hydrogen-sulfide adsorption agent (A1) with hydrogen in the fuel gas to sulfurate hydrodesulfurization catalyst precursor (P1) and to form hydrodesulfurization catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-generating unit (4)    Water supply unit (7)
NOVELTY - The utility model relates to industrial use pneuma equipment field, specifically a propane filter, comprising shell, pedestal, spiral tube and a filter, a spiral tube and a filter are the internal setting in shell, upper end of the spiral pipe provided with a air inlet pipe to the external shell, said filter comprising a bracket and filter cloth, the filter cloth is covered at upper end of external bracket, a filter provided with a air outlet pipe to the external shell, the gas outlet pipe provided with a pressure-reducing valve and stop valve, lower part of the shell and shell internal connected is provided with a liquid outlet pipe, the liquid outlet pipe provided with a switch valve, the top part of shell provided with a hanging ring, shell fixed at a pedestal, on the pedestal set with fork device wherein. The utility model is new type structure is simple, cost is low, a good effect, saves energy and is convenient for hanging a forklift, and comprises the application prospect.
NOVELTY - The utility model relates to the industrial use pneuma equipment field, specifically claims a propane edulcoration device, comprising a shell, a chassis, a spiral pipe and a filter, a spiral tube and a filter are the internal setting in shell, the upper end of the spiral pipe provided with an air inlet pipe to the shell outside, the filter comprising a bracket and filter cloth, the filter cloth is covered at upper end of external bracket, a filter provided with an air outlet pipe to the shell outside, the air outlet pipe is provided with a pressure-reducing valve and stop valve, the lower part of the shell and shell internal connected is provided with a liquid outlet pipe, the liquid outlet pipe is provided with a switch valve, the shell is fixed on a chassis, a bottom chassisis provided with a standing brake universal wheel. The utility model structure is simple, cost is low, edulcoration effect is good, it saves energy and is convenient to move, with popularization and application prospect.
NOVELTY - Recovering lignin solids, comprises (i) hydrolyzing pretreated lignocellulosic feedstock by using an enzyme mixture comprising at least one cellulase enzyme, to obtain a hydrolyzed slurry comprising glucose and lignin solids, where the hydrolysis process is carried out in presence of a polymer that binds or associates with lignin solids; (ii) carrying out solid-liquid separation for recovering lignin solids from a stream comprising lignin solids and polymer; and (iii) collecting process stream comprising recovered lignin solids resulted from solid-liquid separation of the step (ii).    USE - The method is useful for recovering lignin solids used in the preparation of alcohol (claimed).    ADVANTAGE - The method can decrease the amount of cellulase enzyme required by more than 60%, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing alcohol using lignocellulosic feedstock, comprising (a) hydrolyzing pretreated lignocellulosic feedstock by using enzyme mixture comprising at least one cellulase enzyme, to obtain hydrolyzed slurry; (b) fermenting glucose, to obtain fermentation beer comprising alcohol, and concentrating alcohol; (c) carrying out solid-liquid separation to recover lignin solids from the stream; and (d) collecting process stream comprising recovered lignin solids resulted from solid-liquid separation of the step (b).
NOVELTY - An ethanol-fermenting yeast mutant strain of genus Scheffersomyces having clotrimazole resistance, is new.    USE - The strain is useful in ethanol fermentation for producing ethanol (all claimed) from lignocellulosic biomass.    ADVANTAGE - The strain has increased ethanol tolerance, furfural tolerance, and vanillin tolerance, and increases ethanol productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing ethanol involves using yeast mutant strain grown in a medium containing corn steep liquor.
NOVELTY - Fuel gas containing sulfur content is circulated with hydrogen to desulfurizer containing hydrodesulfurization catalyst precursor (P1) including phosphorus and nickel in upstream, and hydrogen-sulfide adsorption agent (A1) including zinc oxide in downstream, and the hydrodesulfurization catalyst precursor is sulfurated into hydrodesulfurization catalyst (C1). Thus, the fuel gas is desulfurized.    USE - Desulfurization of fuel gas. The desulfurized fuel gas is used in system for producing hydrogen for fuel cell system (all claimed).    ADVANTAGE - The fuel gas is desulfurized by economical method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of desulfurization catalyst;    (2) desulfurization system (20), which has desulfurization unit (3) for removing sulfur content from fuel gas containing sulfur content, and fuel supply unit (2) which supplies fuel gas to the desulfurization unit. The desulfurization unit has hydrodesulfurization catalyst precursor (P1) and hydrogen-sulfide adsorption agent (A1); and    (3) hydrogen production system (30), which has desulfurization system and hydrogen-producing unit (4) which generates hydrogen from fuel gas desulfurized in desulfurization unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Fuel cell system (1)    Fuel supply unit (2)    Desulfurization unit (3)    Hydrogen-producing unit (4)    Desulfurization system (20)    Hydrogen production system (30)
NOVELTY - Reduction of the diolefin and oxygenate content of a liquefied 2-5C hydrocarbon, involves feeding the liquefied hydrocarbon to a vessel containing a solid adsorbent disposed on a support thus adsorbing the diolefins and oxygenates on the adsorbent.    USE - The process and apparatus are useful for reducing the diolefin and oxygenate content of a liquefied 2-5C hydrocarbon (claimed).    ADVANTAGE - The process and apparatus can be efficiently used in removing impurities upstream of the amine absorber without disturbing the overall liquefied petroleum gas (LPG) treating operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for reducing the diolefin and oxygenate content of a liquefied 2-5C hydrocarbon, which comprises: a first conduit in fluid communication with a liquefied hydrocarbon source and a vessel, the vessel comprising solid adsorbent disposed on a support, the adsorbent suitable for adsorbing diolefins and oxygenates; and a second conduit in fluid communication with the vessel for receiving the liquefied hydrocarbons of reduced diolefin and oxygenate content from the vessel.
NOVELTY - Producing pentaderivatives and/or alpha , beta -unsaturated decenals, comprises (a) fermentatively producing 1-butanol, 2-butanol or isobutanol, (b) dehydrating obtained butanols to butenes, (c) optionally separating obtained butenes, when butenes are present as a mixture in isobutene, butene-1, butene-2 or a butene mixture comprising butene-1, cis-butene-2 and trans-butene-2, (d) lengthening obtained butenes, and (e) optionally further derivatizing obtained pentanal or pentanal mixture, reacting pentanal or pentanal mixture to alpha , beta -unsaturated decenals, and and optionally further reacting.    USE - The method is useful for producing pentaderivatives and/or alpha , beta -unsaturated decenals (claimed).    ADVANTAGE - The method makes use of renewable and non-renewable natural resources.
NOVELTY - The new type utility claims a closed culture dish, wherein the closed culture dish comprises and a dish cover which can be tightly buckled with the dish bottom; the dish bottom comprises a dish bottom wall and a bottom wall, cover comprises cover wall and a cover wall; on the dish bottom side wall and a cover side wall contact surface is provided with friction sealing device is limited out air tightness of the contact surface. The stable air component the cover wall is equipped with hole or small hole way, using micro-pore filter membrane and inner hole plug is set in hole way, or filter by using the small leather by determining its structure as the gas exchange channel, can maintain lumen of culture dish, keeping balance out air pressure in the culture dish to prevent cracking of a bottom and a cover, too can filter through the air, in culture dish to prevent disease microorganism is bacteria or spore equal harmful gas sol shape through the diffusion layer and pollute and ensures safety of the operator.
NOVELTY - Composite particle comprises a core, a protective shell encasing the core, a tendril layer, and several polymeric chains attached to the protective shell.    USE - Composite particle is useful for recovering microorganisms, preferably microalgae which produces biofuel from aqueous medium preferably drinking water (all claimed). The composite particle is also useful for isolating other microorganisms such as bacteria and fungi which are in various applications such as in pharmaceuticals, food, supplements, and fuel. The composite particle is useful as a coagulation agent.    ADVANTAGE - The polymer composite coagulation agents rapidly and efficiently concentrate microalgae from growth medium under external magnetic field. The composite particle is reusable, thus reducing the cost. The composite particle enables to efficiently harvest microorganisms like microalgae, and has little or no adverse impact or interference on downstream processes or common processing steps performed on microorganisms. The composite particle can be mass-produced at low cost. The method requires little or no post-harvest processing in order to remove chemicals, reagents, or materials and involves a de-watering step which requires little maintenance, results in high concentration factors, consumes little energy, and may be operated continuously. The particles enable recovery of microorganisms from solution without additional mechanical or chemical processing. The composite particle produces well-defined polymer structures by inherent flexibility of reversible addition-fragmentation chain transfer (RAFT) polymerization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method of recovering a microorganism from a solution.
NOVELTY - Manufacture of low temperature protective agent comprises uniformly mixing polybutylene, benzoic acid, polyphenol and glacial acetic acid, stirring, adding potassium fulvate and liquid paraffin, stirring, and standing; adding Chinese mosla herb, welsh onion stalk, ginger, and pine needle into sealed container, adding 75 wt.% ethanol, performing infiltration for 12 hours, adding 75 wt.% ethanol, soaking, collecting percolate, adding 75 wt.% ethanol, heating, and recovering ethanol; dissolving glycerol in extract, heating to 40-50 degrees C, and sterilizing.    USE - Method for manufacturing low temperature protective agent used for crop (claimed).    ADVANTAGE - The method is simple and convenient to use, has anti-freezing effect, and reduces damage on trees.
NOVELTY - Processing caffeine mother liquor involves pumping caffeine mother liquor former polyethylene mother tank using in centrifugal pump, where mother liquor is pre-heated using plate heat exchanger at 35-40 degrees C. The pre-heated mother liquor from former tank is concentrated and then concentrated liquor is pumped into later polyethylene tank through film. The concentrated liquor is evaporated and finally crystallized by centrifugation process.    USE - Method for processing caffeine mother liquor (claimed).    ADVANTAGE - The method enables to process caffeine mother liquor in simple, convenient, cost-effective and eco-friendly manner by consuming less energy.
NOVELTY - Processing sludge involves constructing a flow channel, where mud is circulated with micro-organism in flow channel for 2-5 hours. The obtained sludge is dehydrated, where dehydrated sludge is fermented at 60-70 degrees C. The fermented sludge is cured at room temperature. The cured sludge is further dehydrated to obtain processed sludge.    USE - Method for processing sludge (claimed).    ADVANTAGE - The method enables to process sludge that converts waste matter into nutrient soil, promotes growth and development, increases yield, soil organic matter content and soil activity, improves soil physical and chemical character and soil plate structure, promotes crop early maturing, crop root system, stem diameter and leaf thickness, and improves drought, water-logging, cold, pest and disease resistance.
NOVELTY - Preparation of aminobenzoyl glutamic acid comprises adding 180 g/mL glutamic acid and p-nitrobenzoyl chloride condensate into aqueous solution, stirring until completely dissolved to obtain 35% aqueous solution of p-nitrobenzoyl glutamate, adjusting pH to 7.3, adding 52 g/mL ammonium chloride, heating to 55 degrees C, adding 63 g/mL gray cast iron powder, heating at 75 degrees C for 2.5 hours, heating at 85 degrees C for 3.5 hours, filtering to remove iron slurry, water washing, decoloring, adding charcoal crystal, filtering, washing and drying.    USE - Method for preparing aminobenzoyl glutamic acid (claimed).    ADVANTAGE - The method increases reaction rate and reduces environmental pollution.
NOVELTY - Method (M1) for preparing a sap involves one or more steps chosen from inactivating microbial fermentation inhibitor contained in sap obtained from oil palm trunk and/or leafstalk of oil palm, separating the microbial fermentation inhibitor, and removing the microbial fermentation inhibitor.    USE - The method is useful for preparing sap which is useful as culture medium for culturing microorganism (claimed), and in ethanol fermentation process.    ADVANTAGE - The method reduces establishment and environmental impact of persistent oil palm industry, and produces useful substances at a higher efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for culturing microorganism using the sap;    (2) method (M3) for producing useful substances involves culturing the microorganism; and    (3) method (M4) for using the sap involves collecting and/or removing the inactivated microbial fermentation inhibitor, adding the collected microbial fermentation inhibitor to fuel, foods and drinks raw material, resin-finishing raw material, resin-finishing material, soil improvement raw material, fertilizer as a fuel, fuel auxiliary component, food and drinks adjuvant, soil improvement raw material, or fertilizer component.
NOVELTY - Producing an organic compound comprises harvesting at least one organic compound from an organism or cell line genetically engineered with a gene for at least one proton-pump protein.    USE - The method is useful for: producing an organic compound that is biologic or fuel, where the biologic is used to treat ankylosing spondylitis, autoimmune diseases, cancer, Crohn's disease, diabetes, gout, indeterminate colitis, inflammatory bowel disease, psoriasis, psoriatic arthritis, rheumatoid arthritis, ulcerative colitis, uveitis and viral infection (all claimed); research, medicine, stem cell research and host organism production, production of food source or natural resource including energy production; and producing spider silk, cartilage and exoskeleton structures.    ADVANTAGE - The method: allows genetically engineered organisms and cells lines to increase the amount of ethanol; increases the proton gradient and available ATP which will then provide the engineered organism or cell line with an abundance of energy to increase production of a biofuel; produces transgenic chicken that requires less feed than a non-transgenic chicken; increases production of various cellular products including fatty acids, amino acids and ethanol; increases ethanol tolerance; decreases toxic effects of ethanol stress, protein aggregation, glucose, glycogen, trehalose, NADH and flavin adenine dinucleotide in hydroquinone form consumption, loss of the proton gradient, and glycolytic negative feedback loop of an organism or cell line; provides organism having maximal amount of surface area to absorb light; and produces higher quality and a higher activity of organic compounds, including biologics and biofuels. No biological data given.
NOVELTY - Plant for producing wood pellets or other solid granulates from small pieces of organic material and/or vegetable origin, comprises devices for feeding, processing, drying, compressing, cooling and discharging the material. The devices are arranged in containers, which are individually transported and modularly combined to form at least a substantial portion of the plant comprising containers. At least one of the devices is arranged in a container having a vertically aligned longitudinal axis.    USE - The plant is useful for producing wood pellets or other solid granulates (claimed).    ADVANTAGE - The plant allows energy-optimized operation of solid granules which are transported with less effort.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the plant.    Raw material inlet unit (1)    Sieve (2)    Wet screening disintegrator (3)    Buffer and dosing device (5)    Drying device (6)
NOVELTY - A municipal sludge recycling processing system, belongs to organic solid waste treatment technology and biomass can technology field. Wherein, comprising in sequence a type garden greening trash pulverizer, a triangular ridge aerobic composting reaction stack, a triangular ridge second level aerobic composting reaction stack, a sieving machine, a triangular ridge aerobic composting reaction stack microorganism microbial inoculum and a sprinkler, a triangular ridge second level aerobic composting reaction stack respectively connected a microorganism microbial inoculum sprayer, earthworm cultivation a biological reactor, earthworm cultivation a biological reactor and fully mixing Anaerobic fermentation tank connection. The utility model is new type of device comprises a complete municipal sludge resource treatment is, taking municipal sludge through a quadratic harmless and recycling treatment, at last conversion as suitable organic fertilizer standard of ministry of agriculture organic fertilizer, a process at the same time a biomass energy, marsh gas and organic fertilizer, and earthworm, set with obvious economic benefit and the environment-friendly social benefit.
NOVELTY - This utility new type is a a novel sludge organic fertilizer production device, a t. c, dewatering machine, a drying and grinding device, a. comprising a fermentation pool, a sludge detector and to pump mud machine,... d to pump mud machine and dewatering machine connected with, said dewatering machine comprises dehydration chamber, mud outlet and drain pipe, a dewatering machine and before drying device has equipped with conveying belt, the drying device comprises drying chamber and has a sludge outlet, the drying device and between milling device has equipped with conveying belt, the grinding device has a motor, motor shaft, rotating shaft and base plate, the motor shaft and fixedly connected with the rotating shaft, the rotating shaft two are equipped with edge has grinding stone wheel, the left side of the bottom plate has material. wherein, the new type high-strength sludge organic fertilizer production device comprises using a high efficiency, low pollute and work is stable.
NOVELTY - Single crystal iron metal-organic framework comprising at least one metal-ligand cluster is new. The metal-ligand cluster comprises metal cluster and at least one ligand having two or more carboxylate groups is new. The metal cluster is substituted iron oxide (I). The single crystal has a size greater than or equal to 10 mu m. The metal organic framework comprises cavities having a free diameter of 4-40 Angstrom and pores having a pore volume of 0.1-4 cm3/g.    USE - The metal-organic framework is useful for storing a gas, where the gas is hydrogen, methane, carbon dioxide or nitrogen (claimed), where methane or hydrogen used for fueling vehicles.    DETAILED DESCRIPTION - Single crystal iron metal-organic framework comprising at least one metal-ligand cluster comprising a metal cluster and at least one ligand having two or more carboxylate groups is new. The metal cluster is substituted iron oxide of formula (I). The single crystal has a size greater than or equal to 10 mu m. The metal organic framework comprises cavities having a free diameter of 4-40 Angstrom and pores having a pore volume of 0.1-4 cm3/g.    X = metal ion comprising Fe, Co, Mn, Zn, Ni, Mg, Cu, or Ca.    An INDEPENDENT CLAIM is also included for single crystal iron metal-organic framework.
NOVELTY - The utility model, belonging to conjugated linoleic acid production technology field, specifically relates to an alcohol recovery device for conjugated linoleic acid production. The alcohol recovery device for conjugated linoleic acid production comprises a primary condenser, a secondary condenser and an alcohol recovery tank, material outlet at top end of primary condenser is connected with material inlet at top end of secondary condenser by material pipe, condensed water outlet I at upper part of secondary condenser is connected with condensed water inlet II at lower part of primary condenser by condensed water pipe; upper part of alcohol recovery tank is provided with condensing coil inside. The alcohol recovery device greatly increases alcohol recovery rate, effectively prevents volatilization and waste of alcohol.
NOVELTY - A Nannochloris sp. strain 424-1 (CCAP 251/10), is new. The Nannochloris sp. strain 424-1 is obtained by mutation-selection after cultivation on media with metronidazole, from a wild strain. The Nannochloris sp. strain 424-1 has ability to grow at light intensities of 100-1100 mu l Em-2S-1, with reduced accumulation of anti-oxidants carotenoids. The Nannochloris sp. strain 424-1 has high competence of specific ecotechnological niches colonization, due to high rate of growth.    USE - The Nannochloris sp. strain 424-1 is useful in carbon dioxide sequestration from industrial emissions or waste water treatment and producing aviation biofuels (claimed).    ADVANTAGE - The Nannochloris sp. strain 424-1 has ability to easily transform lipid or free fatty acid into biofuel.    DETAILED DESCRIPTION - A Nannochloris sp. strain 424-1 (CCAP 251/10), is new. The Nannochloris sp. strain 424-1 is obtained by mutation-selection after cultivation on media with metronidazole, from a wild strain. The Nannochloris sp. strain 424-1 has ability to grow at light intensities of 100-1100 mu l Em-2S-1, with reduced accumulation of anti-oxidants carotenoids. The Nannochloris sp. strain 424-1 has high competence of specific ecotechnological niches colonization, due to high rate of growth, between 0.275-0.4 optical density (OD)/day, and short doubling time of 1-3 days. The Nannochloris sp. strain 424-1 forms phycocenosis, with high efficiency in carbon dioxide sequestration from industrial emissions or waste water treatment. The Nannochloris sp. strain 424-1 resists to high concentrations, of 7% and higher, of carbon dioxide in the aeration gases and tolerates high concentrations of salts, particularly sodium bicarbonate/sodium carbonate. The Nannochloris sp. strain 424-1 has ability to grow together with beneficial bacteria and can also be used to sequestrate carbon dioxide through cultivation on epurated wastewater, with concomitant reduction of nitrogen and phosphorus level.
NOVELTY - Method for producing, from algae, a biomass oil and a biofuel oil each comprising at least one product, involves (a) growing an algal culture capable of producing alkenones and co-products, (b) harvesting and dehydrating the algal culture to produce a dry culture, (c) extracting the dry culture with a substantially pure non-polar solvent to produce an extraction mixture of algal biomass and biofuel oil, and (d) separating the extraction mixture into a biomass fraction and a biofuel oil fraction.    USE - The method is used for producing, from algae, biomass oil and biofuel oil each comprising at least one product (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) alkenone-enriched alga strain which when extracted by the method yields greater than 3 wt.% alkenone content with respect to the algae, where the alkenone-enriched alga strain is non-naturally occurring;    (2) genetically modified alga strain which when extracted by the method yields greater than 5 wt.% alkenone content with respect to the algae;    (3) method for producing alkenone derivatives from algae; and    (4) method for producing from algae a first alkenone-enriched sample and a second sample enriched with an other commercially useful product.
NOVELTY - Co-production of co-products involves formulating hydrogen rich syngas stream (S1) with syngas generator (24), subjecting a portion of hydrogen rich syngas stream (S1) to hydrogen separator unit to provide a purified hydrogen by-product stream and hydrogen rich syngas stream (S2), subjecting a portion of hydrogen rich syngas streams (S1) and/or (S2) to a carbon dioxide removal operation to obtain purified hydrogen rich syngas stream and a carbon dioxide by-product stream, catalytically converting the purified hydrogen rich syngas stream to synthesize the hydrocarbons.    USE - Co-production of co-products e.g. methanol, ammonia and urea (all claimed) used for hydrocarbon synthesis.    ADVANTAGE - The method enables efficient and economical co-production of co-products with high yield.    DETAILED DESCRIPTION - Co-production of valuable products from by-products of a process for synthesizing hydrocarbons, involves formulating hydrogen rich syngas stream (S1) with a syngas generator, subjecting a portion of the hydrogen rich syngas stream (S1) to a hydrogen separator unit to provide a purified hydrogen by-product stream and hydrogen rich syngas stream (S2), subjecting a portion of hydrogen rich syngas stream (S1), and/or portion of the hydrogen rich syngas stream (S2), to a carbon dioxide removal operation to obtain purified hydrogen rich syngas stream and a carbon dioxide by-product stream, catalytically converting the purified hydrogen rich syngas stream to synthesize the hydrocarbons, and converting the purified hydrogen by-product stream and/or the carbon dioxide by-product stream into valuable co-products.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining hydrocarbon synthesis.    Natural gas supply (12)    Pre-treatment unit (20)    Carbon dioxide removal stage (21)    Syngas generator (24)    Syngas (26)
NOVELTY - Method for preparing microbial fertilizer, involves (a) selecting microbial strains, (b) inoculating the microbial strains into fermentation medium, and performing culturing process to obtain microbial fermentation broth, (c) adding the microbial fermentation broth into precipitation tank, adding flocculating agent, and centrifuging obtained mixture to obtain precipitate comprising concentrated microbial fermentation broth, (d) pumping the microbial fermentation broth into adsorption tank for performing adsorption, and (e) drying obtained product.    USE - The method is useful for preparing microbial fertilizer (claimed).    ADVANTAGE - The method is cost-effective to perform, and consumes less time.    DETAILED DESCRIPTION - Method for preparing microbial fertilizer, involves (a) selecting microbial strains, (b) inoculating the microbial strains into fermentation medium comprised in a fermentation tank, and performing culturing process to obtain microbial fermentation broth, (c) adding the microbial fermentation broth into precipitation tank, adding flocculating agent, and centrifuging obtained mixture to obtain precipitate comprising concentrated microbial fermentation broth, (d) pumping the microbial fermentation broth into adsorption tank to obtain powder for performing adsorption, and (e) drying the powder using flash dryer to obtain highly concentrated powder of microbial fertilizer.
NOVELTY - Plant comprises (a) a hydrogen generation unit (10) for producing hydrogen, (b) a hydrogen storage device (15) for storing hydrogen, comprising a loading unit (14) for loading a support medium with hydrogen generated in the hydrogen generation unit, and a discharging unit (19) for discharging the hydrogen of the loaded support medium, (c) a heat generation unit (4) for generating heat, and (d) a heat storage unit for storing the heat generated by the heat generating unit. The heat storage unit is connected with the discharge unit.    USE - The plant and the method are useful for storing energy (all claimed).    ADVANTAGE - The plant improves availability of electrical power generated from renewable energy sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for storing energy, comprising producing hydrogen by the hydrogen generation unit, loading the support medium with the hydrogen generated in the hydrogen generation unit by the loading unit, storing the loaded support medium by the support medium storage unit, generating heat by the heat generating unit, storing heat generated by the heat generation unit by the thermal storage unit, discharging the hydrogen of the loaded support by the discharging unit, and providing heat by the thermal storage unit in the discharge unit, where the heat is for discharging hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the plant.    Heat generation unit (4)    Hydrogen generation unit (10)    Loading unit (14)    Hydrogen storage device (15)    Discharging unit (19)
NOVELTY - The sensor has a generator electrode (6) arranged in a detector electrode (5). A control circuit (9) is connected with the generator electrode to continuously operate the detector electrode and to hold potential-controlled negatively reduction voltage with respect to loosened environment oxygen, active oxygen radicals and ions to take off the oxygen radicals and ions with a primary product by stored chemical reaction and oxidization at the detector electrode. A current measurement unit measures current at the detector electrode.    USE - Electrochemical sensor for detecting gas or vapor of a target substance.    ADVANTAGE - The control circuit is connected with the generator electrode to continuously operate the detector electrode with respect to the oxygen radicals and ions to take off the oxygen radicals and ions with the primary product by the chemical reaction and oxidization at the detector electrode, thus operating the sensor in a simple manner and detecting gas or vapors of the target substance in a continuous and stable manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of an electrochemical sensor.    Counter electrode (1)    Housing cover (2)    Detector electrode (5)    Generator electrode (6)    Control circuit (9)
NOVELTY - The system has electronic pressure controller (4) which is provided with gas phase detector (5). The chromatographic column (2) is provided with phase splitter (3). The gas phase detector is connected in parallely with connection shunt, electronic pressure controller and phase splitter. The samples fed to the column are separated. The separated sample is delivered to the gas phase detector under the action of the electronic pressure controller.    USE - Multi-channel sampling system of gas chromatography.    ADVANTAGE - The various components of compounds are analyzed fastly and effectively. The flexibility of the device is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for atmosphere detecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-channel sampling system of gas chromatography.    Chromatographic column (2)    Phase splitter (3)    Electronic pressure controller (4)    Gas phase detector (5)    Hydrogen flame ion detector (6)
NOVELTY - Preparation of biological diesel oil emulsion comprises adding or mixing single emulsion biodiesel with alcohol demulsifier, centrifuging to obtain clear biodiesel and water phase, and separating oil and water.    USE - Method for preparation of biological diesel oil emulsion (claimed).    ADVANTAGE - The method has good breaking effect, mostly recovers and recycles the demulsifier, and it does not damage the property of biological diesel oil and introduce other impurities into biodiesel system.
NOVELTY - Increasing sweet corn yield comprises taking cattle manure-feeding earthworm, cleaning, soaking in water, stirring, centrifuging, precipitating, filtering, adding spraying liquid and spraying.    USE - Method for increasing sweet corn yield (claimed).    ADVANTAGE - The method is safe, ecological and environment-friendly. The product has improved nutrition value and extended harvest period.
NOVELTY - The preparation method of organic fertilizer from straw involves: (a) carbonizing straw into straw charcoal; (b) crushing straw charcoal to obtain charcoal particle; (c) mixing dry chicken manure particles and fresh chicken manure in a mass ratio of 10:1, then adding decomposition agent and deodorant, transferring material to a well, adding water, fermenting under controlled ventilation and drying to obtain a dry mixed chicken manure powder; (d) mixing straw charcoal powder with dry chicken powder, adding beneficial agents and molding aid, and stirring well.    USE - Method is useful for preparing organic fertilizer from straw (claimed).    ADVANTAGE - The method enables environmentally-friendly preparation of organic fertilizer with improved product quality.    DETAILED DESCRIPTION - The preparation method of organic fertilizer from straw involves: (a) carbonizing straw into straw charcoal; (b) crushing straw charcoal to obtain charcoal particle; (c) mixing dry chicken manure particles and fresh chicken manure in a mass ratio of 10:1, then adding decomposition agent and deodorant, transferring material to a well, adding water, fermenting under controlled ventilation for 7-15 days, and drying to obtain a dry mixed chicken manure powder; (d) mixing 50-55 wt.% straw charcoal powder with 40-45 wt.% dry chicken powder, adding 0.0l-1 wt.% beneficial agents and 1-4 wt.% molding aid, stirring well, adding 5% acetic acid solution and mixing; and (e) granulating mixture of organic manure in pelletizer to obtain granules with diameter of 3.5-5.5 mm, and packing.
NOVELTY - Fermentation agent comprises 6x 107-8x 107 colony-forming unit (CFU)/g Bacillus licheniformis, 2x 107-4x 107 CFU/g Bacillus coagulans, 2x 107-4x 107 Bacillus megaterium, 300-350 enzyme unit (U)/g neutral protease, 200-250 U/g laccase, 0.1-0.15 wt.% sodium acetate trihydrate and 0.4-0.45 wt.% calcium chloride.    USE - Fermentation agent used for reducing chicken manure coliform bacteria (claimed).    ADVANTAGE - The fermentation agent has 99% coliform bacteria removal rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of fermentation agent comprising mixing raw materials, chicken manure and cassava residue, and fermenting at natural conditions.
NOVELTY - Trichoderma biological humic acid comprises Trichoderma hyphae and spores, Trichoderma metabolites, biological humic acid, fulvic acid and amino acid, nucleic acid, gibberellic acid, indole acetic acid, cellulose, and lignin.    USE - Trichoderma biological humic acid used for preventing and treating diseases of crops.    ADVANTAGE - The Trichoderma biological humic acid is a green, bio-organic type fertilizer, and improves soil micro-environment of wood mold biological humic acid and its products.    DETAILED DESCRIPTION - Trichoderma biological humic acid comprises Trichoderma hyphae and spores, Trichoderma metabolites, biological humic acid, fulvic acid and amino acid, nucleic acid, gibberellic acid, indole acetic acid, cellulose, and lignin. It is prepared by mixing the raw materials, crushing , and carrying out degradation treatment with alkali or ammonia to obtain the degradation products; adding 0.02-0.1 wt.% Trichoderma and 50-60 wt.% water, mixing, carrying out aerobic or anaerobic fermentation at 20-35 degrees C for 5-7 days to obtain the Trichoderma biological humic acid. The Trichoderma is Trichoderma wood or Trichoderma green mold.
NOVELTY - Expelling insects of vegetable in vegetable greenhouse comprises (i) observing, and recording the kind of vegetables and corresponding vegetable pest; (ii) choosing the smoky substances, which includes chili, cumin and plant stem end; (iii) planting the vegetables in container, which is placed within greenhouse; (iv) connecting a reference line to the center of the shed door at both ends of the greenhouse; (v) mixing smoke and grass frusta, and combusting for 1-3 hours; and (vi) opening the shed door for 20-40 minutes and then shutting the door.    USE - The method is useful for expelling insects of vegetable in vegetable greenhouse (claimed).    ADVANTAGE - The method eliminates plant diseases and insect pests and does not pollute the environment.    DETAILED DESCRIPTION - Expelling insects of vegetable in vegetable greenhouse comprises (i) observing, and recording the kind of vegetables and corresponding vegetable pest; (ii) choosing the smoky substances, which includes chili, cumin and plant stem end; (iii) planting the vegetables in 3-7 m2 container, which is placed within greenhouse; (iv) connecting a reference line to the center of the shed door at both ends of the greenhouses; where the reference line in the container is multi-arc-shaped line and is arrayed on both sides of the reference line; (v) mixing smoke and grass frusta, and combusting for 1-3 hours; and (vi) opening the shed door for 20-40 minutes and then shutting the door.
NOVELTY - Preparing carbamorph involves dehydrating morpholine in presence of an organic solvent to obtain carbamate that is heated, crushed and modulated. The obtained product is complexed with mancozeb and zinc in presence of organic solvent to obtain dehydrated crystal that is packaged.    USE - Method for preparing carbamorph (claimed).    ADVANTAGE - The method enables to prepare carbamorph that ensures reduced decomposition, pollution and generation of harmful impurity and dust, and requires no product drying process to save from fire accident generation.
NOVELTY - Preparation of ethoxyethyl ether comprises using organic solvent to prepare oxyfluorfen ethyl ether and oxyfluorfen ether acetate distillation dehydration process product, mixing, injecting with carrier solvent through spray film evaporator, carrying out dehydration process, wet grinding, modulating, packaging, dehydrating zinc and mancozeb complex in organic solvent and performing crystal transformation process.    USE - Method for preparing ethoxyethyl ether (claimed).    ADVANTAGE - The method is safe and environment-friendly.
NOVELTY - A wet product mix of monosultap is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain monosultap.    USE - Preparation of monosultap (claimed).    ADVANTAGE - The method enables preparation of monosultap, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparation of promacyl comprises mixing organic solvent and promacyl wet product, distilling to carry out dehydration, spraying into film evaporator, heating or distilling to carry out dehydration, wet grinding, modulating, and packaging; and adding mancozeb and zinc complex dissolved in organic solvent, and performing crystal dehydration process.    USE - Method for preparation of promacyl (claimed).    ADVANTAGE - The method reduces decomposition of harmful impurity and dust pollution, and avoids fire accident generation in product drying process.
NOVELTY - A wet product mixture containing carbosulfan is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or distillation-dehydrated in heating-film evaporator, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and organic solvent is added to mixture, and dehydration-crystal transformed, to obtain carbosulfan.    USE - Preparation of carbosulfan (claimed).    ADVANTAGE - The method enables preparation of carbosulfan, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparation of thiram comprises mixing organic solvent and distilled dehydrated wet product, heating or film-evaporating, wet grinding, modulating, continuously packaging, and simultaneously performing dehydrated crystal transformation process of mancozeb and zinc complex in organic solvent.    USE - Method for preparing thiram (claimed).
NOVELTY - Preparing furamethrin comprises (a) taking organic solvent and furamethrin wet product, distilling and dehydrating, (b) taking solvent as a carrier, injection heating or through film evaporator, distilling and dehydrating, wet grinding, transforming, continuously packaging and (c) adding mancozeb and zinc simultaneously into the crystal complex, dehydrating and transforming crystal in the organic solvent.    USE - The method is useful for preparing furamethrin (claimed).    ADVANTAGE - The method: reduces the pollution of harmful impurities and dust; reduces decomposition of the products; avoids fire accidents during product drying process.
NOVELTY - A wet product mix containing dibromophosphorus is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is dehydration-crystal transformed, to obtain dibromophosphorus.    USE - Preparation of dibromophosphorus (claimed).    ADVANTAGE - The method enables preparation of dibromophosphorus, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Processing tolclofos-methyl comprises (i) mixing an organic solvent used in preparing tolclofos-methyl and tolclofos-methyl wet product, distilling and dehydrating; (ii) heating or heating, distilling and dehydrating through a film evaporator, wet grinding, modulating and packaging; and (iii) complexing in mancozeb and zinc containing organic solvent, dehydrating and carrying out crystal transformation.    USE - The method is useful for processing tolclofos-methyl (claimed).    ADVANTAGE - The method reduces decomposing of product, avoids fire accident in drying process and reduces generation of harmful impurities and dust.
NOVELTY - Preparing iprobenfos complex involves dehydrating iprobenfos using organic solvent, where solvent as the carrier is injected through heating or film evaporator distillation process. The dehydrated product is complexed with mancozeb and zinc using organic solvent to obtain product that is crushed, wet ground, modulated and packaged.    USE - Method for preparing iprobenfos complex (claimed).    ADVANTAGE - The method enables to prepare iprobenfos complex that ensures reduced decomposition, pollution and generation of harmful impurity and dust, and requires no product drying process to save from fire accident generation.
NOVELTY - A wet product mix containing fenitrothion is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydrating-crystal transformed, to obtain fenitrothion.    USE - Preparation of fenitrothion (claimed).    ADVANTAGE - The method enables preparation of fenitrothion, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparing kayaphos comprises (i) mixing organic solvent and wet product of kayaphos, distilling, and dehydrating; (ii) taking the solvent as a carrier, subjecting to injection heating process or heating, distilling, and dehydrating through a film evaporator to enable the dehydration process and wet smashing process, modulating, packaging, and continuously operating; and (iii) complexing mancozeb and zinc complex in the organic solvent, dehydrating, and transforming crystals.    USE - The method is useful for preparing kayaphos (claimed).    ADVANTAGE - The method: reduces the decomposition products, reduces pollution caused by harmful impurities and dust; and avoids the occurrence of fire accident during product drying process.
NOVELTY - Poultry excrement plowing roller comprises ring (1), protective rubber (2), turn rake teeth (3), left and right connecting plate (4), pull rod (5) and reinforcing support (6). The turn rake teeth is lengthwise mutually staggered, and is connected with left and right connecting plate. The left and right connecting plate of the hoop prevents work when a brush touches fermentation pool wall of protective rubber.    USE - Poultry excrement plowing roller.    ADVANTAGE - The poultry excrement plowing roller is simple, economic and easy to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of poultry excrement plowing roller.    Ring (1)    Protective rubber (2)    Turn rake teeth (3)    Left and right connecting plate (4)    Pull rod (5)    Reinforcing support (6)
NOVELTY - Preparing organic fertilizer involves fermenting waste filler containing natural plant saponins, and active sludge in mass ratio of 1:1-5 in a tank containing water at 10-50 degrees C for 7-30 days at low stirring speed in anaerobic condition (dissolved oxygen level of 2-6mg/l) to obtain product.    USE - Method for preparing organic fertilizer (claimed).
NOVELTY - Preparing fertilizer involves mixing fresh chicken manure, grass meal (or other organic matter), complex enzyme and corn flour to obtain mixture. The mixture is composted at 60-80 degrees C for 1 day. The mixture is heated next day to kill Escherichia coli, pest and insect eggs. The mixture is deodored in second day to eliminate smell of chicken manure. The mixture is loosely dried on third day to obtain white hypha on fourth day. The dried material is flavored with yeast and then fermented for fifth to seventh day. The fermented material is dried and packaged.    USE - Method for preparing fertilizer (claimed).
NOVELTY - Compost turning machine comprises pedestal (1) and main body (2) that is connected with supporting frame (3). The left end of main body is set with stirring device (4). The middle unit of main body is set with cylinder (5) that is connected with main body terminal. The another end of main body is connected with pedestal for lifting main body.    USE - Compost turning machine.    ADVANTAGE - The compost turning machine is safe, durable and efficient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of compost turning machine.    Pedestal (1)    Main body (2)    Supporting frame (3)    Stirring device (4)    Cylinder (5)
NOVELTY - Fermentation pool comprises angle iron, which is welded by a frame (1) with a pulling plate (2). Angle iron carriage (3) is welded on the angle iron at inner side and the frame are mounted on a base (13), rotating shaft (12), belt pulley, left and right excrement throwing impellers. Right excrement throwing impeller is located in the left excrement throwing impeller. The frame is provided at back of a scraping plate, which is mounted on the left and right excrement throwing impellers and the rotating shaft. Manure baffle plate is lifted from its middle position to form exit.    USE - Fermentation pool used for cleaning poultry excrement (claimed).    DETAILED DESCRIPTION - Fermentation pool comprises angle iron, which is welded by a frame with a pulling plate. Angle iron carriage is welded on the angle iron at inner side and the frame are mounted on a base, rotating shaft, belt pulley, left and right excrement throwing impellers. Right excrement throwing impeller is located in the left excrement throwing impeller. The frame is provided at back of a scraping plate, which is mounted on the left and right excrement throwing impellers and the rotating shaft. Manure baffle plate is lifted from its middle position to form exit, where lifting plate outlet height of the angle iron and pulling distance of plate groove is 250-350mm.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation pool.    Frame (1)    Pulling plate (2)    Angle iron carriage (3)    Rotating shaft (12)    Base (13)
NOVELTY - The method involves pressing a feeding unit by a mass flow meter pressing sleeve type reactor through a hydrogen pressure reducing valve. Hydrocarbon fraction oil raw material in a raw material tank is fed into the mass flow meter pressing sleeve type reactor by a pneumatic feeding pump. An inner layer is utilized for filling catalyst. An outer layer is divided into a pre-heating section, a constant temperature section and a cooling section. A liquid level of a liquid product is controlled in a product storage tank by a pneumatic control valve.    USE - Hydrocarbon fraction hydrogenation testing method.    ADVANTAGE - The method enables utilizing a catalyst bed layer to simulate actual production of an industrial device, ensure stable control, high product quality and provide stable and reliable test data for light hydrocarbon fraction hydrogenation removing thermodynamics and dynamics research of alkyne and olefin reaction process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hydrocarbon fraction hydrogenation testing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a hydrocarbon fraction hydrogenation testing method.'(Drawing includes non-English language text)'
NOVELTY - A hybridoma cell line (CGMCC NO. 7459) is new.    USE - The hybridoma cell line is useful for producing a monoclonal antibody that binds human alpha -LA. The monoclonal antibody that binds human alpha -LA is used in the manufacture of a kit for detecting alpha -LA in milk (all claimed).    ADVANTAGE - The monoclonal antibody that binds human alpha -LA is used for rapid, easy and environment-friendly alpha -LA detection with high sensitivity and specificity. The monoclonal antibody has high purity and titer, and no cross-reactivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a monoclonal antibody that binds human alpha -lactalbumin ( alpha -LA), secreted by the hybridoma cell line above; and    (2) a method for preparing the monoclonal antibody of (1) by immunizing the BALB/c mice with alpha -LA, screening and selecting positive clones by enzyme linked immunosorbent assay (ELISA), subcloning to obtain stable hybridoma cell lines secreting the antibody that binds to alpha -LA, and purifying the antibodies using affinity chromatography.
NOVELTY - Cooling machine comprises a front tube (1), which is provided with tube feed tank (2). The tube feed tank is sleeved that has a roller (3) and, roller is mounted at the bottom front tube. The roller is provided with supporting roller (4).    USE - Cooling machine.    ADVANTAGE - The cooling machine has simple structure and is convenient to use, stable and reliable and saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cooling machine.    Front tube (1)    Tube feed tank (2)    Roller (3)    Supporting roller (4)
NOVELTY - This utility new type relates to a planting organic garbage, comprising a fermentation chamber, the fermentation chamber is mounted water bath, a fermentation cabin provided with a shape of a cylinder, the two side provided with a used for for discharging for a hollow shaft, the hollow shaft and the connected roller, a hollow shaft mounted b the water bath groove a, the roller inner wall provided with a plurality of spiral guide plate, the hollow shaft can not only used for fixing fermenting chamber, can as feed wherein and discharging wherein, fully use resource, multiple spiral guide plate set with b a fermentation chamber, the fermentation chamber rotating spiral guide plate to rotate to make the organic waste fully stirring, reduces fermentation time of microorganism, structure is simple, the operation cost is low, the occupied space is small, using waste, organic waste for conversion is organic fertilizer again using, effective reduce pollute environment.
NOVELTY - This utility new type claims a organic fertilizer A degradation device, comprising degrading groove, stirrer, stirring shaft, electric heater, hot oil (water) pipe, a speed reducer, a transmission belt, motor and; stirrer equipped with a transverse centre position of degrading groove, stirrer stirring shaft by the rotary stirring of a fixed, stirring shaft part is degrading groove extending outside a speed reducer, a belt with a speed reducer, upper end lower end... degrading groove by the first cavity and the second cavity one, the first cavity in degrading groove, rectangular cavity by the lower part and upper part of cylinder is composed of cavity, the second cavity is set in interlayer cavity outside of the first, the second inner containing cavity has temperature exchange medium as a liquid. Equipped with a stirring system and heating system greatly increase the fermentation efficiency of use and strain rate of raw material, so as to reduce the organic fertilizer production time, full closed reaction, reduces the putrid.. pollute environment in a great extent, at the same time of whole device is convenient for automatic management.
NOVELTY - The reactor (1) has a muffle tube (17), in which the fuel to be gasified (36) is received. The muffle tube has an upper muffle tube portion (19) in a vertical axis direction, while forming an annular gap (20) in a lower region of the reactor. The upper region of the reactor is received in a muffle housing (21) such that the gas escaping from the muffle tube, in the muffle housing-side annular gap, enters in a lower muffle tube end (18).    USE - Reactor for gasification of fuels, particularly of solid carbonaceous fuels, such as biomass or waste materials, particularly wood or similar materials.    ADVANTAGE - The upper region of the reactor is received in a muffle housing such that the gas escaping from the muffle tube, in the muffle housing-side annular gap, enters in a lower muffle tube end, and hence ensures obtaining the improved gas quality in conjunction with high fuel flexibility in a simple and functionally reliable manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for gasification of fuels, particularly biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a reactor. (Drawing includes non-English language text).    Reactor (1)    Muffle tube (17)    Lower muffle tube end (18)    Upper muffle tube portion (19)    Annular gap (20)    Muffle housing (21)    Fuel to be gasified (36)
NOVELTY - The device (100) has a sewer port (110) for loading the organic feedstock in a pressure chamber (115) and a conveyor (120). The conveyor is provided for impinging the feedstock with conveying gas which has a higher temperature than the feedstock introduced in the pressure chamber. Another sewer port (130) is provided for loading of feedstock heated by the conveying gas from the pressure chamber into the gasification plant. The conveyor uses carbon dioxide as conveying gas.    USE - Device for introducing solid organic feedstock, particularly wood chips in a gasification plant (Claimed).    ADVANTAGE - The device has a sewer port for loading the organic feedstock in a pressure chamber and a conveyor for impinging the feedstock with conveying gas, which has a higher temperature than the feedstock introduced in the pressure chamber, and hence ensures effective and reliable supply of feedstock in the gasification plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for introducing solid organic feedstock in a gasification plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an organic feedstock introducing device.    Organic feedstock introducing device (100)    Sewer ports (110,130)    Pressure chamber (115)    Conveyor (120)    Gasification plant (200)
NOVELTY - Separating nitrogen and methane comprises filling an adsorbent bed with flexible material TUTCH-1 or TUTCH-2 as an adsorbent, and taking as an adsorbent, controlling inlet pipeline and adsorbent bed temperature and constant pressure, adding methane and nitrogen mixed gas into the adsorbent bed, where the flexible material adsorbs methane gas.    USE - The method is useful for separating nitrogen and methane component (claimed).    ADVANTAGE - The method: ensures smooth and stable mixed gas flow rate; ensures collection of low methane in the feed gas without any loss; has low investment; is simple and convenient; and removes and provides high purity nitrogen, thus increasing methane gas concentration (more than 98%), which can be directly used as liquefied natural gas (LNG) or natural gas for vehicles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for separating nitrogen and methane mixture, comprising methane/nitrogen mixed raw material gas storage tank (1), first adsorption bed (2), a second adsorption bed (3), methane tank (4) and nitrogen tank (5). The outlet of the methane/nitrogen mixed raw material gas storage tank is connected to the inlet of a quality control meter. The first and second adsorption beds are parallel and respectively equipped with a temperature groove. The first and second adsorption bed is filled with flexible material TUTCH-1 or TUTCH-2 as adsorbent. The inlet of the two absorption bed is connected to the outlet of the quality control meter. The outlets of the adsorption bed are connected with a back pressure valve. The methane tank and nitrogen tank are connected via the back pressure valve. The front and rear sides of the first and second adsorption beds are provided with an elastic buffer layer made of porous polyethylene fiber material. The adsorption bed adsorption column has an inner diameter of 1 cm and adsorption column length of 15 cm.
NOVELTY - A reversible hydrogen storage material comprises magnesium-zinc borohydride-metallic composite (I).    USE - Reversible hydrogen storage material is used for hydrogen fuel cell.    ADVANTAGE - The reversible hydrogen storage material has excellent thermal stability.    DETAILED DESCRIPTION - A reversible hydrogen storage material comprises magnesium-zinc borohydride-metallic composite of formula: MgxZn1-x(BH4)2-M (I), where x is 0.05-0.95 and M is palladium, platinum or cobalt. An INDEPENDENT CLAIM is included for preparation of reversible hydrogen storage material.
NOVELTY - Microbial fertilizer comprises 0.01-0.02 pts. wt. enzymatic micro-organism, 23-30 pts. wt. stone powder, 60-70 pts. wt. carbon powder, 0.01-0.02 pts. wt. caterpillar fungus powder, 0.01-0.02 pts. wt. Bacillus powder, 12-16 pts. wt. ammonium dihydrogen phosphate, 60-70 pts. wt. corn straw, 40-50 pts. wt. soybean straw, 8-10 pts. wt. monocalcium phosphate, 1-8 pts. wt. phosphorite powder and 20-30 pts. wt. oyster shell powder.    USE - Microbial fertilizer used for promoting plant growth (claimed).    ADVANTAGE - The microbial fertilizer improves plant immunity, and inhibits harmful bacteria growth in soil.
NOVELTY - Bio-fertilizer comprises 50-60 pts. wt. soybean pulp, 10-12 pts. wt. castor, 8-10 pts. wt. non-glutinous rice starch, 50-60 pts. wt. Azolla, 1-2 pts. wt. borax, 2-3 pts. wt. activated carbon, 20-25 pts. wt. sweet potato starch, 3-4 pts. wt. peat, 5-7 pts. wt. pea vine, 8-10 pts. wt. sweet potato vine, 10-13 pts. wt. straw, 20-30 pts. wt. urea, 3-4 pts. wt. Artemisia rupestris, 2-3 pts. wt. Bidens tripartita, 1-2 pts. wt. Ligusticum sinense, 3-5 pts. wt. vermiculite powder, 3-4 pts. wt. effective microorganisms and water.    USE - Bio-fertilizer used for increasing soil fertility.    ADVANTAGE - The bio-fertilizer is nutritious, increases disease resistance, nutrient, yield and quality, and improves the soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-fertilizer, which involves:    (A) frying Ligusticum sinense, Bidens tripartita and Artemisia rupestris in a pan and then grinding into powder;    (B) adding water with powder to carry out extraction to obtain extract;    (C) mixing remaining components uniformly with the extract and then fermenting in a sealed container for 20-30 days; and    (D) drying the fermented product in a dryer, and then granulating to obtain final product.
NOVELTY - Producing biodiesel comprises mixing short-chain alcohols with an activator to form an activated short chain alcohol; mixing oil and activated short-chain fatty alcohol, heating, and stirring to form alcohol ester mixed solution; adding the alcohol ester mixed solution into a piston compressor, forming a reaction interface, quickly completing transesterification via a porous solid acid catalyst plate, to form fatty acid ester; and carrying condensation recovery of short chain alcohol, and carrying out continuous rotary separation to recover fatty acid esters and glycerol by-product.    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The method avoids environment pollution, which greatly increases conversion rate of oil ester to biodiesel oil, and carries out continuous and clean process.    DETAILED DESCRIPTION - Producing biodiesel comprises (i) mixing short-chain alcohols with an activator in the mass ratio of 2:0.01-0.1, and forcibly dispersing to form an activated short chain alcohol by dispersing machine; (ii) mixing oil and activated short-chain fatty alcohol in the molar ratio of 1:1-1.5, heating to 40-60 degrees C, and stirring for 13-20 minutes so as to form alcohol ester mixed solution; (iii) adding the alcohol ester mixed solution into a piston compressor, shearing under high pressure, forming a reaction interface of alcohol ester mixed solution, quickly completing transesterification via a porous solid acid catalyst plate, to form fatty acid ester; and (iv) releasing the pressure in the outlet channel of a piston compressor containing fatty acid ester, excess short-chain alcohols and glycerol byproduct, passing into the rotary separator, carrying condensation recovery of short chain alcohol, and carrying out continuous rotary separation to recover fatty acid esters and glycerol by-product.
NOVELTY - Loop-mediated isothermal amplification (LAMP) primer composition comprises forward inner primer FIP comprising fully defined 46 nucleotides (SEQ ID NO: 1) as given in the specification, reverse inner primer BIP comprising fully defined 38 nucleotides (SEQ ID NO: 2) as given in the specification, positive outside primer F3 comprising fully defined 18 nucleotides (SEQ ID NO: 3) as given in the specification, reverse outside primer B3 comprising fully defined 20 nucleotides (SEQ ID NO: 4) and reverse loop primer LB comprising fully defined 24 nucleotides (SEQ ID NO: 5).    USE - The LAMP primer composition is useful for detecting Phytophthora drechsleri (claimed).    ADVANTAGE - The method has high accuracy, high sensitivity, specificity and convenient operation, realizes constant temperature amplification and early identification of pathogens, reduces pesticide use and production cost for pesticide, and is environmentally friendly.    DETAILED DESCRIPTION - Loop-mediated isothermal amplification (LAMP) primer composition, comprises forward inner primer FIP comprising fully defined 46 nucleotides (SEQ ID NO: 1) as given in the specification, reverse inner primer BIP comprising fully defined 38 nucleotides (SEQ ID NO: 2) as given in the specification, positive outside primer F3 5'-gtgatcctttcaccctgg-3' (SEQ ID NO: 3), reverse outside primer B3 5'-ttacaaatgtcagctggatg-3' (SEQ ID NO: 4) and reverse loop primer LB 5'-tgtacgtctacagaggatttggat-3' (SEQ ID NO: 5). An INDEPENDENT CLAIM is also included for detecting Phytophthora drechsleri, comprising extracting DNA from the microorganism to be detected, taking DNA as template and carrying out LAMP using the LAMP primer composition, and observing the reaction solution for color change, where the presence of blue color indicates positive result and the presence of purple color indicates negative result.
NOVELTY - An organic fertilizer preparing method involves composting organic waste slurry at 40-70 degrees C for 4 weeks in first stage and at 30-40 degrees C for 2-3 months in second stage. The obtained composite is polished by using a trommel machine and a specialized polishing machine followed by adding 110-140 mg/l sodium bicarbonate with the composite, stirring, aliquoting and packing the mixture to obtain a finished product.    USE - Method for preparing organic fertilizer.
NOVELTY - Pot process involves carrying out in-situ diazotization and subsequent hydrolysis of substituted aniline in presence of nonpolar nonprotic organic solvent at temperature of more than ambient temperature. The generated effluent is partially recycled without purification or pretreatment in diazotization and subsequent hydrolysis.    USE - Pot process used for preparing substituted phenol. Uses include but are not limited to dye, fuel additive, agrochemical product, and pharmaceutical intermediate for abafungin, oxymetazoline and vortioxetine.    ADVANTAGE - The substituted phenol is prepared by economical, quick, environmentally-friendly, easy and safe pot process with reduced usage of water content and energy consumption.
NOVELTY - Use of algae for the efficient processing of typical domestic wastewater by separation in eutrophic lakes, where the algae strain is Scenedesmus quadricauda SDEC-8 having a preservation number of CCTCC No: M 2014448.    USE - The Scenedesmus SDEC-8 algae are useful for the efficient processing of typical domestic wastewater, preferably in eutrophic lake; for the purification of nitrogen and/or phosphorus-containing waste water; and for the prodcition of lipid, fatty acid, protein, starch, cellulose, polysaccharide and/or nucleic acid.    ADVANTAGE - The Scenedesmus SDEC-8 algae can be efficiently used in the removal of nitrogen and phosphorus, and obtaining biological diesel oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) use of a Scenedesmus SDEC-8 solution to give four Scenedesmus SDEC-8 cells; and (2) a method of culturing four Scenedesmus, comprises the steps of: (a) inoculating four Scenedesmus SDEC-8 in sterile culture medium BG11; (b) preparation of artificial wastewater; and (c) inoculating the resulting four Scenedesmus SDEC-8 seed in the sewage culture medium.
NOVELTY - Composting device comprises a tube for receiving composting materials. The tube is perforated to define spaced apertures for connecting an internal space of the tube with an outside of the composting device.    USE - Used as a composting device.    ADVANTAGE - The composting device, preferably an in-ground composting device: provides a continuous feed of compost and nutrients to the surrounding soil, and requires little additional work from a user to enrich the soil; and naturally attracts worms to its location which further provides an additional level of soil enrichment that is not provided by conventional out-of-ground composting devices.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a composting assembly comprising the composting device, a cap for covering one end of the tube and a plunger;    (2) a composting kit comprising several tubes, each of which are of a different diameter such that the tubes can be nested within each other; and    (3) a second composting device for inserting into the ground, comprising a hollow container having an internal space, where the container comprises at least one upper first opening for receiving composting material into the internal space and at least one second opening for connecting the internal space of the container with the ground surrounding the composting device in use.
NOVELTY - Treating liquid sewage sludge, liquid waste from industry and/or agricultural waste, comprises mixing the mixture of sewage sludge and filler material thoroughly and subjecting to automated fermentation using aeration, at 50-70 degrees C to increase sugars, proteins, starches, nitrates, carbondioxide, ammonia and amino acids, removing degradable fraction of cellulose and lignin, reducing the rate of aeration and slowly cooled to 35-50 degrees C and obtaining material with moisture content of 55 wt.%.    USE - The method is useful for treating liquid sewage sludge, liquid waste from industry and/or agricultural waste used to produce biofuels, especially for electricity production or heat.
NOVELTY - Earthworm cultivation matrix and its preparation method are claimed. The earthworm cultivation matrix comprises 1-3 pts. wt. rice bran, 4-6 pts. wt. weed, 4-6 pts. wt. straw, and 8-10 pts. wt. dairy manure. The preparation method involves cutting straw and weed into sections having length of 5-10 mm, and adding remaining raw materials, uniformly mixing mixture, adding 0.1-0.2% edible yeast to water, spray mixture on above-prepared mixture, performing fermentation process, adding fermented product to plant soil in a ratio of 1:3-5, and stacking and drying mixture.    USE - The matrix is useful for cultivating earthworm (claimed).    ADVANTAGE - The matrix enables to promote growth and development of earthworm.
NOVELTY - A Lactobacillus plantarum strain CCFM382 (CGMCC 9734), is new.    USE - The L.plantarum strain is used in preparation of leavening agent for reducing acrylamide content in starchy foods and preparing bread with reduced acrylamide content (all claimed).    ADVANTAGE - The strain enables to reduce acrylamide content by simple and cost-effective method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) leavening agent prepared using the L.plantarum strain; and (2) method for reducing acrylamide content in starchy foods, involves adding 108-1010 colony forming units (CFU) L.plantarum to 100 g dough, preparing food products using dough, and maintaining at 120 degrees C.
NOVELTY - Fertilizer for saline soil comprises weathered coal, microorganisms, manure, straw, ferrous sulfate, lees, nitrogen fertilizer, phosphorus fertilizer and potash fertilizer. The microorganisms include nitrogen-fixing bacteria, phosphorus solubilizing bacteria, potassium solubilizing bacteria, fermentative bacteria and photosynthetic bacteria.    USE - As fertilizer for saline soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) mixing straw and manure, adding 5-6% ferrous sulfate, mixing uniformly, and fermenting mixture, (b) adding weathered coal, microorganisms, and lees to fermented mixture, mixing uniformly, and granulating mixture, and (c) adding nitrogen fertilizer, phosphorus fertilizer and potash fertilizer to granules obtained in step (b), and mixing uniformly to obtain the product.
NOVELTY - Fertilizer comprises 100-120 pts. wt. chicken manure, 40-60 pts. wt. pig manure, 40-60 pts. wt. diatomite, 8-10 pts. wt. azone (RTM: laurocapram), 50-60 pts. wt. bamboo peel, 20-30 pts. wt. rice bran, 30-40 pts. wt. flour, 10-12 pts. wt. bone powder, 15-17 pts. wt. Lagochilus inebrians, 18-20 pts. wt. oriental arborvitae, 20-40 pts. wt. green foxtail, and 155-175 pts. wt. water.    USE - The fertilizer is useful for Gardenia (claimed).    ADVANTAGE - The fertilizer is rich in nutrients, and environmentally-friendly, and promotes root growth of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing and uniformly mixing the above-mentioned raw materials, fermenting mixture for 2-4 days and granulating fermented product.
NOVELTY - Producing marsh gas by fermenting crop straw and vegetable waste, involves (a) chopping crop straw and vegetable waste into pieces having size of 3-5 cm, (b) pretreating crop straw by mixing chopped crop straw in lime solution, incubating mixture at 20-25 degrees C for 3-6 days, then adding calcium hydroxide, and controlling moisture content of straw at 50-65%, (c) mixing the crop straw and vegetable waste, introducing inoculum to mixture, performing anaerobic fermentation at 30-37 degrees C for 50 days, and performing controlled fermentation.    USE - The method is useful for producing marsh gas by fermenting crop straw and vegetable waste (claimed).    ADVANTAGE - The method is rapid.    DETAILED DESCRIPTION - Method for producing marsh gas by fermenting crop straw and vegetable waste, involves (a) chopping crop straw and vegetable waste into pieces having size of 3-5 cm, (b) pretreating crop straw by mixing chopped crop straw in lime solution, incubating mixture at 20-25 degrees C for 3-6 days, then adding calcium hydroxide, and controlling moisture content of straw at 50-65%, (c) mixing the crop straw and vegetable waste in a ratio of 6:1-14:1, introducing inoculum to mixture, performing anaerobic fermentation at 30-37 degrees C for 50 days, where volume of inoculum is 15-35%, and performing controlled fermentation with total solid concentration of 10-16%.
NOVELTY - Culture method for anaerobic digestion of food waste sludge involves adding raw materials to 1 g/l activated carbon, and 1 g/l Aspergillus niger, performing culturing process, where the raw material is added before 10-15 days of culturing process, and adding nutrients chosen from potassium, phosphorus, magnesium and other elements, 1360 mg/l dipotassium phosphate, 444 mg/l calcium chloride, and 500 mg/l magnesium sulfate to fermentation broth.    USE - The culture method is useful for anaerobic digestion of food waste sludge (claimed).
NOVELTY - This utility new type relates to a improvement of a biological nest, especially one used for a process to make the sewage purification is a, a is a plurality piece columnar bar rubber are integrally formed using a ball, the lower end surface of a sphere provided with spoiler, and wave form b side, to make the sphere can not only generate vortex water flow, it can flow along the rotating, at the same time a by a wave plate is for stacking biological film, and this ball b is set has a plurality of through-hole, the thalli can be a inner a biological nest, and between this ball by a good tightness, stable effective water level and a long flow in inner water tank, would not be damaged, use life is long.
NOVELTY - A healthcare Scoparia dulcis soap comprises 150-300 g purified water, 50-100 g sodium hydroxide, 300-350 g coconut oil, 150-200 g Hawaiian nut oil, 100-150 g jojoba oil, 50-100 g linseed oil, 100-150 g avocado oil, 8-15 g lavender essential oil, 80-100 g S. dulcis, 30-50 g Tenuifolia, 40-50 g self-heal, 20-30 g Rhizoma coptidis, 40-50 g Indigo naturalis, and 20-30 g dahurian patrinia herb.    USE - A healthcare S. dulcis soap for prevention and treatment of eczema (claimed).    ADVANTAGE - Process is environment-friendly, and product is safe to use, relieves itching and skin erosion, diminishes inflammation, promotes cell regeneration, balances oil secretion, soothes sensitive skin, eliminates sore, stops bleeding, and has no toxic side effect and allergic reaction, antibacterial effect, fragrance, and anti-ulcer effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of healthcare S. dulcis soap which involves mixing purified water and sodium hydroxide into stainless steel container, stirring until no solid particle, cooling at 55 degrees C to obtain alkali solution, heating coconut oil, Hawaiian nut oil, jojoba oil, linseed oil, and Avocado oil into stainless steel boiler, stirring for 30 minutes, dripping lavender essential oil for 15 minutes, stirring, standing, cooling at 55 degrees C to obtain oil solution, grinding S. dulcis, Tenuifolia, self-heal, R. coptidis, I. naturalis, and dahurian patrinia herb into 80 meshes fine powder using grinding machine, mixing to obtain powder, stirring alkali solution and oil solution for 60 minutes, adding mixed powder, continuously stirring for 15 minutes, pouring into mold, standing for 7 days, demolding, and packaging.
NOVELTY - Producing 11alpha-hydroxy-1,4-androstadiene-3,17-dione involves performing fermentation by inoculating phytosterol-producing Mycobacterium with Aspergillus niger with phytosterols to obtain the product.    USE - Method for producing 11alpha-hydroxy-1,4-androstadiene-3,17-dione from Aspergillus niger (claimed).    ADVANTAGE - The method enbales to extract 11alpha-hydroxy-1,4-androstadiene-3,17-dione in a highly efficient, economical, and environment-friendly manner.
NOVELTY - The antioxidant additive comprises oleaginous doped sabura additive and citric acid to slow down oxidation and degradation processes of biofuel. The sabura base additive is extracted from pollen produced by Tetragonista angustula bees and citric acid.    USE - Antioxidant additive for use in biodiesel (claimed).    ADVANTAGE - The antioxidant additive increases induction period and useful life of the biofuel, and offers renewable, sustainable and environment friendly source of additive, and thus improves income and lives of beekeepers.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting advantages of the natural antioxidant additive sabura base for use in biodiesel. (Drawing includes non-English language text).
NOVELTY - The system has a biomass distribution hopper, biomass conveyors and a biomass container arranged in sequence manner. A syngas delivery pipes system is arranged in an inner side of the biomass container. A side of the biomass container is connected to the biomass-feeding hopper. The biomass conveyors are formed as screw-type conveyors.    USE - Continuous-feed-type biomass pyrolysis system.    ADVANTAGE - The system can use excess heat generated by pyrolysis process for treating heat-exchange and materials transformation in the pyrolysis process. The system has zero emission and environmental friendly operation, while achieving economic improvements.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a continuous-feed-type biomass pyrolysis system.
NOVELTY - Composition comprises mixture of procymidone and iprodione as active component.    USE - The composition is useful for controlling gray mold of vegetables, flowering plants and other crops.    ADVANTAGE - The composition is prepared cost-effectively, environmentally-friendly as it causes no pollution to environment, and safe for human and livestock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the composition, which involves (a) mixing the active components with auxiliary component except deionized water using high speed mixer, and stirring obtained mixture, (b) adding the mixture to high speed sand mill, adding deionized water to the high speed sand mill, and crushing obtained mixture for 8 hours, and (c) filtering suspension obtained in step (b), adding the suspension to storage tank, maintaining the suspension at static condition for 4 hours, and packaging obtained product.
NOVELTY - The machine has a forming machine body provided with a spiral conveying mechanism (1), a paper around cloth mechanism (2), a glue forming mechanism (3) and a cutting mechanism (5). The paper around cloth mechanism is provided with a paper plate (21) and a paper tape (22). The paper plate is connected with the paper tape and the cutting mechanism. A glue forming mechanism is connected with a cyclo sealing part (33). The glue forming mechanism is connected with a paper forming machine.    USE - Moxa column making rolling forming machine.    ADVANTAGE - The machine improves production quality and efficiency and avoids pollution, and is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a moxa column making rolling forming machine.    Spiral conveying mechanism (1)    Paper around cloth mechanism (2)    Glue forming mechanism (3)    Cutting mechanism (5)    Paper plate (21)    Paper tape (22)    Cyclo sealing part (33)
NOVELTY - Preparing hand sanitizer, comprises (i) adding sodium dodecyl dimethyl betaine, coconut fatty acid diethanolamide, alpha -phenylphenol, methyl paraben and water into a blender, and stirring; and (ii) adding traditional Chinese medicinal extract, honeysuckle extract and rosemary essential oil, and continuously stirring for 20-30 minutes, and adjusting pH to 6-7, stopping the stirring process, cooling to room temperature, and packaging, where the traditional Chinese medicinal extract includes Artemisia leaf, pomegranate rind, Aloe, Rheum officinale and radix scutellariae.    USE - The method is useful for preparing hand sanitizer (claimed).    ADVANTAGE - The method is simple, economical, and environmental friendly.    DETAILED DESCRIPTION - Preparing hand sanitizer, comprises (i) adding 4-9 pts. wt. sodium dodecyl dimethyl betaine, 15-25 pts. wt. coconut fatty acid diethanolamide, 0.1-1 pts. wt. alpha -phenylphenol, 0.5-3 pts. wt. methyl paraben and 40-55 pts. wt. water into a blender, and stirring at 30-45 degrees C for 10-20 minutes; and (ii) adding 15-20 pts. wt. traditional Chinese medicinal extract, 1-5 pts. wt. honeysuckle extract and 0.1-0.8 pts. wt. rosemary essential oil, and continuously stirring for 20-30 minutes, and adjusting pH to 6-7, stopping the stirring process, cooling to room temperature, and packaging, where the traditional Chinese medicinal extract includes Artemisia leaf, pomegranate rind, Aloe, Rheum officinale and radix scutellariae.
NOVELTY - The heater has a transfusion tube wrapped by a physical heating tube. An upper end of a hanging rope is connected with a fixed terminal.    USE - Light industry transfusion heater for a patient.    ADVANTAGE - The heater has simple manufacture process and energy saving effect, and is practical and convenient to use and environment-friendly, and increases comfort of the patient and reduces environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a light industry transfusion heater.
NOVELTY - The device has reaction container whose sides are connected to a water outlet groove (7) which is equipped with an inflow groove (3) to which a source water tank (1) is connected. A fixing pole is arranged in reaction container whose lower side is set with elastic filler (5), stainless steel cathode plate and titanium alloy anode plate. The top end of anode plate is connected to connecting frame and cathode plate. An aeration head (8) is arranged at the bottom of reaction container and is provided between cathode and anode plates equipped with three phase separator.    USE - Electrochemical coupling type biological organic waste water processing device.    ADVANTAGE - The aeration head is arranged at the bottom of reaction container and is provided between cathode and anode plates equipped with three phase separator, such that the organic waste water processing is performed efficiently. The sewage treatment is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrochemical coupling type biological organic waste water processing device.    Source water tank (1)    Inflow groove (3)    Elastic filler (5)    Water outlet groove (7)    Aeration head (8)
NOVELTY - The system has cylindrical casing which is divided by clapboard into anaerobic area (4), full time domain biochemical treatment area (7), and dissolved air dross area (11). A sewage pipe (1) is attached to the anaerobic area which is connected to full time domain biochemical treatment area through elbow (3). The biochemical treatment area is provided with hollow telescopic pole (5) wound with chain filler (6) containing PVC and is connected to the dissolved air dross area containing dissolved air machine (9).    USE - Full-time domain rural sewage treatment system.    ADVANTAGE - The solid-liquid separation of the waste water can be performed efficiently, so that the sewage can be treated easily. The temperature of the full time domain biochemical treatment area can be increased. The aerobic fermentation can be performed rapidly. The survival rate of composite flora can be increased and the removing rate of pollutant can be improved. The installation property of the system can be improved, so that the system can be installed conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the full-time domain rural sewage treatment system.    Sewage pipe (1)    Elbow (3)    Anaerobic area (4)    Hollow telescopic pole (5)    Chain filler (6)    Full time domain biochemical treatment area (7)    Dissolved air machine (9)    Dissolved air dross area (11)
NOVELTY - Automatic integrated ecological septic tank comprises manure pipe (1), anaerobic settling zone (4), hollow rod (5), chain (6), continuous biochemical treatment area (7), floating ball (10), outlet pipe (12), groove (13), water outlet pipe (14), aeration pipe (15), water-gas separation chamber (16), motor (18), cylindrical pipe (19), air inlet pipe (20), ventilation pipe (21) and air hole (22).    USE - Automatic integrated ecological septic tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of automatic integrated ecological septic tank.    Manure pipe (1)    Anaerobic settling zone (4)    Hollow rod (5)    Chain (6)    Continuous biochemical treatment area (7)    Floating ball (10)    Outlet pipe (12)    Groove (13)    Outlet pipe (14)    Aeration pipe (15)    Water-gas separation chamber (16)    Motor (18)    Cylindrical pipe (19)    Air inlet (20)    Ventilation pipe (21)    Air hole (22)
NOVELTY - Water quality modifying agent comprises 15-30 pts. wt. nano-silver, 30-50 pts. wt. medical stone powder, 5-15 pts. wt. betaine, 20-40 pts. wt. Bacillus, 20-35 pts. wt. photosynthetic bacteria, 25-45 pts. wt. oxygen-enriching agent, 1-5 pts. wt. potassium dihydrogen phosphate, 2-6 pts. wt. sodium nitrophenolate and 0.15-0.55 pts. wt. broken yeast wall powder.    USE - Used as a water quality modifying agent.    ADVANTAGE - The modifying agent can not only absorb toxic pollutants in the water body, and improve the water body environmental conditions, and quality of water sludge, but also can provide nutrient substances required by fish, and thus promotes healthy growth of fish, and increases the aquaculture production yield.
NOVELTY - Preparing short-chain volatile fatty acids involves inoculating sludge into kitchen garbage as fermentation substrate and then mixing to obtain fermentation matrix. Polyglycoside is added into fermentation matrix and then fermented under anaerobic condition to obtain the product.    USE - Method for preparing short-chain volatile fatty acids (claimed).    ADVANTAGE - The method enables to prepare short-chain volatile fatty acids with high yield in a cost-effective manner, and recycles food waste, and disposes food waste safely.
NOVELTY - The system has the cubes (17) that are provided with the holes to allow passage of the liberated gases to the oxygen and hydrogen pipes (8,9). The stoppers (26,27) are provided to prevent a downward flow of a liquid from the heat exchange chambers (10,11) to a solution container (1) through the gas pipes. The cubes with holes are placed in the heat exchange chambers to allow passage of the liberated gases through the holes to the pipes and inside the heat exchange chambers between an electrolyte (7) and a ceiling of heat exchange chamber.    USE - System for producing hydrogen gas and oxygen gas through electrolysis.    ADVANTAGE - The cubes are provided with the holes to allow passage of the liberated gases to the oxygen and hydrogen pipes and placed in the heat exchange chambers to allow passage of the liberated gases through the holes to the pipes and inside the heat exchange chambers between an electrolyte and a ceiling of heat exchange chamber. Thus, greater safety is provided to the system against the combustibility and volatility of the liberated hydrogen gas. Hence, the amount of hydrogen and oxygen produced is increased while ensuring safe production of hydrogen. The positive terminal of the direct current (DC) supply is fed to the anode and negative terminal of the DC supply is fed to the cathode so that the heated water in hydrogen heat exchange chamber and oxygen heat exchange chamber is allowed to flow to the solution container. Thus, the temperature of the water in the solution container is maintained effectively while reducing the amount of energy required to be spent to maintain the temperature of the water within the solution container.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the system for producing the hydrogen and oxygen gases through electrolysis.    Solution container (1)    Electrolyte (7)    Oxygen and hydrogen pipes (8,9)    Heat exchange chambers (10,11)    Cubes (17)    Stoppers (26,27)
NOVELTY - An electrode catalyst comprises a carrier containing an electroconductive oxide including tin, antimony, niobium, tantalum and/or titanium, and an oxide catalyst having an oxygen defect and including group 4 element and/or group 5 element, supported on the carrier.    USE - Electrode catalyst is used in water electrolysis apparatus (claimed).    ADVANTAGE - The electrode catalyst uses an oxide catalyst which is stable under high potential and exhibits sufficient activity with respect to oxidation of water. The oxide contained in the carrier has high surface area and electroconductivity, and is stable even under high electric potential even if it is not a non-precious metal oxide. The electrode catalyst is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water electrolysis apparatus (100) consisting of an anode including the electrode catalyst, and a cathode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the water electrolysis apparatus.    Water electrolysis apparatus (100)    Solid polymer electrolyte membrane (110)    Cathode catalyst layer (120)    Anode catalyst layer (130)    Gasket (170)
NOVELTY - A recombinant polypeptide comprising an amino acid sequence that is at least 80% identical to the amino acid sequence of fully defined 868 amino acids (SEQ ID NO: 2) or fully defined 852 amino acids (SEQ ID NO: 3), given in the specification, where the polypeptide has beta-glucosidase activity, is new.    USE - The recombinant polypeptide and methods are useful for producing composition, for producing a beta-glucosidase, and for hydrolyzing a lignocellulosic biomass substrate (all claimed).    ADVANTAGE - The recombinant polypeptide and methods have improved efficacy or capability and can be efficiently applied in degrading or hydrolyzing lignocellulosic biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a composition comprising the recombinant polypeptide, and one or more other cellulases;    (2) a recombinant nucleic acid encoding the recombinant polypeptide;    (3) an expression vector comprising the recombinant nucleic acid in operable combination with a regulatory sequence;    (4) a host cell comprising the expression vector;    (5) a method of producing a beta-glucosidase, comprising: culturing the host cell in a culture medium, under suitable conditions to produce the beta-glucosidase; and    (6) a method for hydrolyzing a lignocellulosic biomass substrate, comprising: contacting the lignocellulosic biomass substrate with the polypeptide, or the composition, to yield a glucose and other sugars.
NOVELTY - This utility new type relates to medical equipment, is a child with a comfortable environment-friendly vein infusion fixing support, comprises supporting body, wherein the supporting body is using wood pulp or paper pulp, it is set with vertical folded edge of the top face and periphery, a top surface by supporting part and part composed of sole, provided with a four finger groove on a supporting palm part, set with 2-3 transverse skid-proof groove in the wrist supporting part, and supporting part is a little lower than the wrist supporting sole part, the sole part supporting side edge and supporting wrist part side at top surface of each supporting body provided with a through with a hole, each of through hole and is installed with sticky-button type binding belt. The utility model is new type green and environment-friendly, comfortable and convenient use, when a valid child transfusion easy to move a needle caused by dislocation, cause medicine liquid input to blood vessel outside, generating liquid, equal swelling and pain, a use when a child hand vein transfusion.
NOVELTY - The device comprises an electrolytic cell for chlor-alkali electrolysis with an anode half cell, and a cathode half cell, where the anode half cell and the cathode half-cell are separated through cation exchange membrane. The cation exchange membrane is arranged in the anode half-cell anode for evolution of chlorine, where the cathode half-cell is arranged with an oxygen-consuming electrode and a conduit for supplying gaseous oxygen in the cathode half cell. A pipe is provided for flushing the cathode half cell with inert gas.    USE - Device for chlor-alkali electrolysis.    ADVANTAGE - The device allows flexible use of electricity in a reduced cost, reduces oxygen consumption in the oxygen-consuming electrode at cell voltage, and facilitates high current supply without supplying oxygen to the oxygen-consuming electrode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for the flexible use of electricity, which involves:    (A) preparing chlorine by chlorine-alkali electrolysis;    (B) supplying oxygen at oxygen-consuming electrode; and    (C) generating high current supply for the oxygen-consuming electrode.
NOVELTY - The system (10) uses a methane sensor assembly at an upper opening of a garbage chute. An ozone generator (5) is located adjacent to a lower opening of garbage chute. An ozone delivery tube is mounted to ozone generator emitting ozone directly into a trash receptable. A control unit coordinates the emission of ozone through ozone delivery tube, when methane sensor assembly records methane concentration measurements of a predetermined parts per million quantity at upper opening of garbage chute.    USE - System for disinfecting and deodorizing garbage chutes, for destroying insects and infection-carrying organisms.    ADVANTAGE - The treatment of waste in garbage chutes of multi-story buildings using effective and safe levels ozone reduces or eliminates harmful methane levels. The methane detector is strategically placed at the top of the garbage chute to detect any residual methane and triggers the corona discharge ozone generator to precisely and safely disinfect and deodorize any remaining methane. The system provides two sensors strategically placed throughout a trash chute to efficiently reduce methane levels by emitting ozone at the first detection of methane levels and also being able to detect and address residual methane levels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the operating environment with connections between bottom ozone generator, top methane detector, and control relay.    Trash shaft (1)    Ozone generator (5)    Methane detector (6)    Control relay (8)    System for disinfecting and deodorizing garbage chutes (10)
NOVELTY - The apparatus (100) has a communicating path (120) that sends out a generated gas connecting two adjacent reactors (110). An introducing unit (130) introduces a source gas into a reactor of a front stage. A cooling unit (150) cools the gas generated with the reactor of front stage at a temperature more and less than the temperatures at which the methanation reaction starts and stops respectively. A water removal unit (160) is provided between cooling unit and reactor of back stage and among one of the communicating paths so as to remove water from the generated gas cooled by cooling unit.    USE - Apparatus for manufacturing methane from hydrogen and carbon dioxide by exothermic reaction.    ADVANTAGE - The water removal unit is provided between cooling unit and reactor of back stage and among one of the communicating paths so as to remove water from the generated gas cooled by cooling unit so that the temperature of reaction zone in the reactor arranged on the next step is reduced, and the producibility of methane or reaction rate of methanation reaction is raised. Thus, the methane is efficiently manufactured at reduced cost while restraining the occupied volume of reactor at minimum and increasing the number of objects of reactor by the simple structure of removing water in the communicating path. Hence, the installation area of methane production apparatus is reduced effectively without changing the capacity of reactor while improving the producibility of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the apparatus for manufacturing methane. (Drawing includes non-English language text)    Apparatus for manufacturing methane (100)    Reactors (110)    Communicating path (120)    Source gas introducing unit (130)    Cooling unit (150)    Water removal unit (160)
NOVELTY - The electrolytic device has housing that includes first and second adjacent flow-through channels which are separated by a first charged barrier having exchangeable ions. The exchangeable ions are capable of passing ions of only one charge, either positive or negative, and blocking bulk liquid flow. The first and second electrodes are in electrical communication with the channels, respectively. A first catalyst is provided in the first channel for combining hydrogen and oxygen gas.    USE - Electrolytic device e.g. suppressor for detecting sample analyte in liquid sample.    ADVANTAGE - By applying the potential across electrodes, the kinetics of ion flow across barrier and capacity are increased, and thus the suppression efficiency of the suppressor device is increased. Detection noise is lowered, since the bubble induced current disturbances are minimized by removing the bubbles. Peroxide concentration in the suppressor device is minimized, so that damage to the ion exchange components within the suppressor is minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for simultaneous electrolysis and catalytic gas elimination in a single electrolytic device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic device including catalyst in two channels of the three channel device.    ERC (10)
NOVELTY - B on the new type utility claims a novel device using cassava alcohol wastewater as raw material for producing gas, the device belongs to biogas production machine field, including, sand (1), regulating pool (2), Anaerobic fermentation tank (3), tank (4), wherein a sand removing groove (1) set with cassava alcohol wastewater inlet (5), impurity outlet (6), sand (1) and regulating pool (2) is provided with a material slurry pump and pipeline (7), a regulating pool (2) and Anaerobic fermentation tank (3) is provided with a material slurry pump and pipe (8). Anaerobic fermentation tank (3) is set with marsh gas fermentation microorganism inlet (9), a material liquid and sediment outlet (10) Anaerobic fermentation tank (3) and water seal (4) is set with pipe (11), tank (4) set with marsh gas outlet (12).
NOVELTY - The utility model of spike and collection well cover is connected by flange and fixed by bolt to prevent the landfill gas. landfill and leachate unite drainage collection well of nail type refuse landfill is distributed in different density and in staggered arrangement onleft and right front and rear hole, which is good for collection of landfill gas. Landfill and leachate unite drainage collection well of nail type refuse landfill, wherein it is united to pump row filling pneuma and filtered liquid. When the small hole leachate collection groove outside wall, collect well leachate lifting in the permeate. N collection well is also set with a degradable liquid discharging pipe, the liquid through pipe conveys to each branch pipe, and then flows into the collection well near the garbage landfill, and the landfill garbage degradation is complete. Percolate collection groove and the nail head are in one whole, the outer diameter of collect well is less than the inner diameter thereof so as to lift the collect well from the nail head . A nail head solid refuses landfill drilling bottom on rectangular pyramid. The utility model landfill gas and leachate a unite pumping, liquid degradable, construction period short, a low cost, a simple structure.
NOVELTY - Device comprises a buffer container (6) arranged adjacent to a fermenter (1), and at least one movably arranged rake (5).    USE - The device is useful for discharging biomass floating layer in fermenter (claimed).    ADVANTAGE - he device discharges biomass floating layer without opening the fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the (Drawing includes non-English language text).    Fermenter (1)    Biomass floating layer (3)    Rake (5)    Buffer container (6)    Guide means (10)
NOVELTY - Styling agent comprises 0.1-20 wt.% strengthening polymer and 0.1-5 wt.% ester compounds (I).    USE - The styling agent is useful in aerosol composition (claimed).    ADVANTAGE - The styling agent exhibits: improved curl retention, preferably high humidity curl retention (claimed), and improved hair feel like grip and combability.    DETAILED DESCRIPTION - Styling agent comprises 0.1-20 wt.% strengthening polymer and 0.1-5 wt.% ester compounds of formula (I).    R1 = -H or -CH3;    R2 = 7-15C alkyl; and    n = 1, 2, 3, 4, 5, 6, 7 or 8.    INDEPENDENT CLAIMS are also included for:    (1) an aerosol composition, comprising a pressure container, and (a) the styling agent and (b) a blowing agent or blowing agent mixture including dimethyl ether, 2,3,3,3-tetrafluoropropene, 1,3,3,3-tetrafluoropropene, propane, propene, n-butane, isobutane, isobutene, n-pentane, pentene, isopentane and/or isopentene, which is located in the pressure container; and    (2) use of (I) for improving curl retention, preferably high humidity curl retention.
NOVELTY - Hairspray comprises a pressure container and an aerosol composition comprising (a) 20-80 wt.% at least one a blowing agent, (b) 0.1-20 wt.% at least one a strengthening polymer and (c) 0.01-5 wt.% ester compounds (I), which are located in the pressure container.    USE - The hairspray is useful in hair styling (claimed).    ADVANTAGE - The hairspray gives hair pleasant feel and well-groomed hair feeling without long-lasting maintenance.    DETAILED DESCRIPTION - Hairspray comprises a pressure container and an aerosol composition comprising (a) 20-80 wt.% at least one a blowing agent, (b) 0.1-20 wt.% at least one a strengthening polymer and (c) 0.01-5 wt.% ester compounds of formula (I), which are located in the pressure container.    R1 = -H or -CH3;    R2 = 7-15C alkyl; and    n = 1-8.    An INDEPENDENT CLAIM is also included for a hair styling, comprising applying the aerosol composition containing (I) on keratin fibers using the blowing agent or blowing agent mixture from the pressure container.
NOVELTY - This new utility model relates to one serial of domestic sewage center circle aeration biological purification device, comprising the biochemical aeration bucket of two or two more than two, microorganism carrier and aeration device. Biochemical aeration bucket is made of plastic barrel, and upper part in biochemical aeration bucket provided with upper bar grate, lower part equipped with the following grate bar, centre provided with centre aeration circulation chamber. Centre of centre aeration circulation room set with aeration pipe. Of bar grate, lower grate bar and center circle chamber composed of annular aeration and microorganism carrier chamber. And microorganism carrier chamber equipped with microorganism carrier. Microorganism carrier is plastic made of multi-leaf multi-way empty shape is spherical shape. The utility model use new biochemical aeration bucket assembly in series to purification device, structure is simple, can consume less equipment investment small, operation cost low, especially increasing center circle aeration pipe, aeration efficiency is high, active sludge, dispersing widely suitable for the city community, plant, school, countryside resident equal discharge requirement of domestic sewage purification.
NOVELTY - This utility new type relates to organic fertilizer preparation technology, in particular, it claims a one organic fertilizer fermentation device, comprising: a., provided with the opposite inlet and outlet wherein, and, b. the pool of turner used for d. b. fermentation pool track to do reciprocating movement is n in the fermentation pool, make fermentation raw material stirring fermentation and gradually from the inlet to the outlet wherein a n in the fermentation pool. This utility new type set with overturning track by fermentation in a double side so as to a turner set. b a a a a a fermentation raw material, b. raw material in a continuous fermentation of throwing, progressive scattering and a certain of displacement, to the fermentation material regularly, in a fermentation pool after a shift, so as to ensure the aerobic fermentation process.
NOVELTY - A disposable taking urine sample the utility new type relates to hospital laboratory collecting the check sample of cup, comprising cup body, wherein urea, part of the cup and provided with outer edge of two symmetrical handle, a pouring urine wherein the adhesive has the outer edge diameter is 0.2 mm of stainless steel silk, and the existing technology, the utility model is new type low cost, convenient use, and for almost without pollute environment.
NOVELTY - The utility model claims a medical appliance, especially a disposable urine collector for checking The a check with a disposable urine, a urine baffle plate, urine collecting groove,, test tubes, wherein the urine baffle plate lower end set with urine groove, urine groove bottom provided with a urine collecting groove bottom groove, urine groove bottom groove side provided with a catheter, a test tube of urine guiding pipe on a test tube plug, a plug side also provided with discharge tube, a test tube plug has a test tube, a urine baffle plate is provided with urine baffle plate opening, in urine baffle opening passes urine l baffle rope. The beneficial effect is: a convenient for the urine collecting automatically, which avoids the urine spraying for a hand over in a urine collection process does not make a large amount of smell, pollute the environment in a process urine after urine collection is sent after the laboratory.
NOVELTY - This utility new type provide a a thio dioxide properties..., a culture dish, evaporating dish, glass bell jar, a rubber plug, a filtering paper and crucible, the top end of a cover glass provided with a plug opening end of glass cover set clock b the culture dish on the inner glass cover left side provided with the evaporating dish, glass bell jar inner side set with crucible, inner crucible provided with soaking the magenta fixing of a filter paper. This utility new type. The beneficial effect is: the experiment device is convenient, time-saving, medicine, intuitionistic, can effective avoid the pollute environment.
NOVELTY - The system has a main water tank (1), an aqueous filter (4), a pump (10), an electronic system control unit (23), and an electric feeding unit (24). The aqueous filter contains distilled water that cleans and distils the hydrogen gas from a separator (3) by passing it through water. The control unit has a programmable logic controller (PLC) software for controlling the predetermined components of the system, an electronic control panel and an analyzer measuring and displaying electric consumption values of the system. The electric feeding unit provides the energy required by the system.    USE - Hydroxy fuel supplement system for use in heating systems. Uses include but are not limited to vehicles, boilers, furnaces and ovens used in houses and cafeterias, and generators for electricity production.    ADVANTAGE - Fuel consumption is reduced, and efficient fuel saving is achieved. Decreases emission values down to around zero, since full combustion is ensured when used with other fuels. Hydroxy fuel supplement system is an environmentally friendly machine.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydroxy fuel supplement system.    Main water tank (1)    Separator (3)    Aqueous filter (4)    Pump (10)    Electronic system control unit (23)    Electric feeding unit (24)
NOVELTY - Composition comprises pimobendan in particulate form coated with a carrier matrix, where the carrier matrix consists of one or more carriers chosen from polyglycolized glycerides and polyethylene glycols (PEGs).    USE - The composition is useful for treating warm-blooded animals, preferably companion animals e.g. dogs (claimed) in treatment of congestive heart failure originating from valvular insufficiency or dilated cardiomyopathy.    ADVANTAGE - The composition enables rapid and substantial dissolution of pimobendan irrespective of pH conditions, and absorbed reliably at all pH conditions representing milieu(s) of the gastrointestinal tract of animals, even if there are considerable pH fluctuations in the gastrointestinal tract, without using an organic carboxylic acid or modifying the crystalline form of the substance, as pimobendan is formed as lipid-embedded particles by applying lipid embedding approach using spray congealing technology. The preparation method is rapid, easily scaled-up, cost-effective and environmentally-friendly as no solvent is required in the formulation and manufacturing process. The oral pimobendan formulation is highly palatable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of a composition involves (a) dispersing particulate pimobendan in a molten carrier matrix, (b) atomizing dispersion obtained in step (a), and (c) cooling and collecting coated particles; and    (2) treatment of warm-blooded animals involves orally administering the composition, one or more excipients, and optionally, one or more further active ingredients chosen from angiotensin converting enzyme (ACE) inhibitors, aldosterone antagonists and/or loop diuretics.
NOVELTY - Sewage treatment device comprises left fixing frame (1) and right fixing frame (12), where fixing frame and left upper part of right frame are set between purification groove (2). The sewage treatment device is also provided with sterilizing device (9). The bottom is set with storage water purification pool (13). The purification groove is set with a baffle plate. The baffle is provided with sewage treatment filler. The purification groove is set with plant mat and equipped with aquatic plant.    USE - Sewage treatment device.    ADVANTAGE - The sewage treatment device ensures low energy consumption, fast disassembling and assembling and convenient use, and is suitable for depth treatment of sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sewage treatment device.    Left fixing frame (1)    Purification groove (2)    Sterilizing device (9)    Right fixing frame (12)    Storage water purification pool (13)
NOVELTY - Preparation of adsorbent comprises mixing sodium silicate or potassium silicate hydrate with distilled water at mass ratio of 1:2 to prepare 20% aqueous solution of sodium silicate or potassium silicate, dropwisely adding 50 wt.% hydrochloric acid at 0-2 degrees C, stirring until pH value is 2-3, taking sol substance, standing at 20-25 degrees C for 1 hour, adding 50 wt.% hydrochloric acid until pH value is 0.6-1.0, adding 20 wt.% ethanol and 8-10 wt.% urea, stirring, standing for 4-5 hours, filtering, washing, drying and calcining at 500-550 degrees C for 5 hours.    USE - Method for preparing adsorbent used for pressure swing adsorption and purification of shale gas (claimed).    ADVANTAGE - The product is renewable and has high-performance, high-capacity and long life.
NOVELTY - A titanium dioxide nanowire array thin film contains fluoride-doped tin oxide (FTO) conductive glass as substrate and titanium dioxide in which titanium dioxide is rutile phase with regular single crystal one-dimensional structure.    USE - A titanium dioxide nanowire array thin film for energy storage and hydrogen production (all claimed).    ADVANTAGE - Energy storage and hydrogen production process is simple, environment-friendly and sustainable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of titanium dioxide nanowire array thin film which involves placing isopropyl titanate-containing hydrochloric acid aqueous solution and FTO conductive glass in hydrothermal tank, performing hydrothermal reaction at 428 K for 1-4 hours, taking out conductive glass, cooling, washing with water, drying, and calcining at 200 degrees C for 2 hours; and    (2) energy storage and hydrogen production which involves placing 2 titanium dioxide nanowire array thin films and platinum (Pt) electrode in 3 tank reactor, adding electrolyte solution, introducing nitrogen (N2) through air drain, connecting electrodes to electrochemical workstation with saturated calomel electrode as reference electrode, connecting electrodes to nanowire array thin films, and irradiating to complete energy storage in thin films and produce hydrogen from working electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a scanning electron microscope image of the nanowire distribution and thickness of titanium dioxide nanowire array thin film.
NOVELTY - Treating sewage involves sewage removing large floating debris through thick grizzly screen and then flowing the obtained material into a collecting tank. The impurity and sand particle from waste water are separated by lifting a vertical sewage pump sewage. The obtained water after separation is entered through a water outlet into an anaerobic pool for performing anaerobic treatment process. The anaerobic treated wastewater is flowed into a biochemical pool. The photosynthetic bacteria, lactic acid bacteria, yeast, gram-positive bacteria and actinomycetes fermentation bacteria are added.    USE - Method for treating sewage (claimed).    ADVANTAGE - The method enables to treat sewage in simple and cost-effective manner, with high efficiency, and has performed degradation of various pollutants effectively, removed odor and reduced pollution load.    DETAILED DESCRIPTION - Treating sewage involves sewage removing large floating debris through thick grizzly screen and then flowing the obtained material into a collecting tank. The impurity and sand particle from waste water are separated by lifting a vertical sewage pump sewage. The obtained water after separation is entered through a water outlet into an anaerobic pool for performing anaerobic treatment process. The anaerobic treated wastewater is flowed into a biochemical pool. The photosynthetic bacteria, lactic acid bacteria, yeast, gram-positive bacteria and actinomycetes fermentation bacteria are added into the biochemical pool. The obtained material is subjected to aerobic treatment and then the treated material is entered into a sedimentation tank. The obtained material is flow into a sterilizing tank.
NOVELTY - Acidic organic fertilizer comprises 20-40 wt.% acidic composite bacterial culture, 15-20 wt.% saponin residue, 15-35 wt.% pine needle, 10-15 wt.% sawdust and straw.    USE - Acidic organic fertilizer used for planting blueberry (claimed).    ADVANTAGE - The acidic organic fertilizer maintains soil porosity and acidity, and ensures increased organic matter content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing acidic organic fertilizer, which involves:    (A) separating acidic composite bacterial culture from acidic soil to obtain humus extract;    (B) filtering obtained extract;    (C) adjusting pH of extract to 1-3;    (D) collecting blueberry root soil to obtain saponin waste water extract;    (E) adjusting pH of extract to 3.5-4.8 for 1-3 minutes to obtain acidified extract;    (F) isolating mycorrhizal fungi in Photinia;    (G) adding bacterium to obtained extract to obtain a mixed bacterial extracts;    (H) mixing mixed bacteria extract with potato dextrose liquid medium to obtain fermentation culture;    (I) mixing fermentation culture and glycerin to obtain parent strains that is stored at -20 degrees C;    (J) mixing saponin waste water extract with ammonia, potassium phosphate and water to obtain saponin residue;    (K) mixing saponin residue with straw, sawdust, pine needles and obtained material;    (L) composting parental strain and sludge compost or fecal material with obtained mixture for 2-3 weeks to obtain mature compost; and    (M) drying composted materials to obtain product that is packaged.
NOVELTY - Nutrient fertilizer comprises 15-25 pts. wt. glucose powder, 12-18 pts. wt. vegetable leaves, 12-17 pts. wt. traditional Chinese medicine residue, 8-13 pts. wt. melon peel, 7-12 pts. wt. bone powder, 1-5 pts. wt. bean cake, 1-3 pts. wt. anthocyanin and 12-17 pts. wt. taomi.    USE - Nutrient fertilizer used for promoting growth of Dianthus caryophyllus.    ADVANTAGE - The nutrient fertilizer is convenient and safe and reliable, and ensures increased survival rate of Dianthus caryophyllus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutrient fertilizer, which involves:    (A) weighing and mixing glucose powder, bone powder, bean cake and anthocyanin;    (B) mixing taomi with obtained mixture to obtain paste;    (C) composting rotten vegetable leaves, traditional Chinese medicine residue and melon peel;    (D) mixing composted mixture and paste to obtain mixture; and    (E) fermenting obtained mixture for 30-36 hours to obtain nutrient fertilizer.
NOVELTY - Composting fertilizer involves mixing 30-40 parts municipal domestic sludge, 20-25 parts plant ash, 5-10 parts straw, 5-10 parts manioc waste and 15-20 parts livestock excrement. The obtained mixture is fermented with 2-5 parts microbial inoculum for 5-7 days. The fermented mixture is cooled to 20-30 degrees C. The cooled material is fermented again with 5-8 parts microbial inoculum for 15-20 days. The obtained mixture is crushed, granulated and dried to obtain product.    USE - Method for composting fertilizer (claimed).    ADVANTAGE - The method enables to compost fertilizer that ensures shortened composting time, no pollution and increased fertilizing effect without peculiar smell.
NOVELTY - Preparing organic fertilizer involves crushing corn straw, soybean straw and melon straw using pulverizer to obtain straw powder that is heated with starch in tank at 90-100 degrees C. The heated material is cooled to 25-30 degrees C. The cooled material is fermented with Bacillus megaterium for 36-40 hours below 30-40 degrees C. The corn straw, bagasse, rice powder, starch and water are crushed in pulverizer to obtain powder that is heated at 50-60 degrees C. The heated material is cooled to 25-30 degrees C. The cooled material is fermented with Bacillus megaterium for 30-40 hours below 30-40 degrees C.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that improves soil structure, increases nutrient utilization, fertilizer effect and crop yield, and ensures low cost preparation, low energy consumption and no pollution.    DETAILED DESCRIPTION - Preparing organic fertilizer involves crushing corn straw, soybean straw and melon straw using pulverizer to obtain straw powder that is heated with starch in tank at 90-100 degrees C. The heated material is cooled to 25-30 degrees C. The cooled material is fermented with Bacillus megaterium for 36-40 hours below 30-40 degrees C. The corn straw, bagasse, rice powder, starch and water are crushed in pulverizer to obtain powder that is heated at 50-60 degrees C. The heated material is cooled to 25-30 degrees C. The cooled material is fermented with Bacillus megaterium for 30-40 hours below 30-40 degrees C. The fermented materials, grass peat, amino acid, calcium superphosphate, potassium sulfate and urea are mixed, where obtained mixture is granulated in twin-screw extrusion granulator. The obtained granules are dried, screened and packaged.
NOVELTY - Synthesis of belinostat involves mixing sodium 3-sulfobenzoate and anhydrous methanol, adding catalytic amount of concentrated hydrochloric acid, reflux heating, concentrating to dryness, adding thionyl chloride, heating at 40-50 degrees C, adding organic solvent, lowering temperature to - 10-10 degrees C, adding aniline, reacting, adding water, stirring, filtering, washing with ether solvent, drying, adding borohydride reducing agent and Lewis acid, stirring, reflux heating, adding solvent, 2-iodoxybenzoic acid and oxidant, stirring, reacting, adding triethyl phosphonoacetate and solubilizer and stirring.    USE - Method for synthesizing belinostat (claimed).    ADVANTAGE - The method shortens production time, improves yield, enhances production safety, reduces environmental pollution and more suitable for industrial production.    DETAILED DESCRIPTION - Synthesis of belinostat comprises mixing sodium 3-sulfobenzoate and anhydrous methanol, adding catalytic amount of concentrated hydrochloric acid, reflux heating, concentrating to dryness, dissolving in alkali A, adding thionyl chloride, heating at 40-50 degrees C, adding organic solvent, lowering temperature to - 10-10 degrees C, adding aniline, reacting, adding water, stirring, filtering, washing with ether solvent, drying, adding borohydride reducing agent, Lewis acid and tetrahydrofuran, stirring, reflux heating, adding solvent, 2-iodoxybenzoic acid and oxidant, stirring, reacting, adding triethyl phosphonoacetate and solubilizer, stirring, adding alkali B, stirring, adding acylating agent, stirring, adding alkali C and hydroxylamine hydrochloride and stirring.
NOVELTY - 2,4 D polyamidine (I) is new.    USE - 2,4 D polyamidine used in preparation of herbicides (claimed).    ADVANTAGE - The method is simple, safe and environment-friendly.    DETAILED DESCRIPTION - 2,4 D polyamidine of formula (I) is new.    n=1-10.    An INDEPENDENT CLAIM is included for preparation of 2,4 D polyamidine.
NOVELTY - Straw processing device comprises a straw, a machine frame (2), a smashing tank (3), a motor (4), a smashing shaft (5), a fermentation tank (7), a heating pipe, a water tank (9), a pressurizing pump (10) and a spraying head (11). The smashing tank machine frame is located at the top of device. Electric machine is connected to smashing tank top center. The smashing knife shaft is placed in electric machine bottom center. The smashing knife shaft is provided with smashing cutter. The fermentation tank is provided with machine frame end. The fermentation tank is surrounded by external wall.    USE - Straw processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw processing device.    Machine frame (2)    Smashing tank (3)    Motor (4)    Smashing shaft (5)    Fermentation tank (7)    Water tank (9)    Pressurizing pump (10)    Spraying head (11)
NOVELTY - Methane generation system comprises a feeding pipe (10), a discharging pipe (20), a fermentation pipeline (30), a straight hydraulic pipeline (31) guarded by a valve, and air resistance plates (38). Fermentation raw material and microbial strain producing methane are inoculated into fermenter under hydraulic pressure to generate methane. The fermenter producing methane moves through convection to a methane storage chamber. The feeding pipe and the discharging pipe, are inserted into the fermenter by the fermentation pipeline.    USE - Methane generation system.    ADVANTAGE - The methane generation system promotes the fermentation of raw materials in the deep fermentation system, and thus improves the methane gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane generation system.    Feeding pipe (10)    Discharging pipe (20)    Fermentation pipeline (30)    Hydraulic pipeline (31)    Air resistance plate (38)
NOVELTY - Methane fermentation system comprises a fermentation pipeline (30), an exhaust pipe (31), a methane gas introducing pipe (32), a discharging pipe (34) provided with a stopper plate, and air resistance plates (38). The methane gas introducing pipe of the methane fermentation system, is provided with a plate (36). Fermentation raw material and microbial strain producing methane are introduced into a fermenter, and processed under hydraulic pressure to generate methane. The generated methane moves by convection in a storage chamber.    USE - Methane fermentation system.    ADVANTAGE - The methane fermentation system promotes the fermentation of raw materials in the deep fermentation system, and thus improves the production of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane fermentation system.    Fermentation pipeline (30)    Exhaust pipe (31)    Methane gas introducing pipe (32)    Discharging pipe (34)    Plate (36)    Air resistance plate (38)
NOVELTY - This utility new type claims a organic fertilizer fermentation a dumper comprises operating table, a tyre, a hydraulic lifter and turn stack pole, said tyre comprises tyre large and small, a small tyre provided with a steering shaft, a steering shaft provided with a transmission stick, the large tyre turning pole and fixedly connected, the operating table by a lifter fixedly connected turn pile pole is above the operating table comprises a seat, a steering wheel protecting cover, a steering wheel through transmission pole and steering shaft rotating connection, one side the operating table is equipped with has engine, engine and turn the stack pole rotating connection, the turning pole horizontal turn stack pole and a longitudinal axis turn stack pole, the horizontal turn stack pole set with arc-shaped blade has a longitudinal axis turn stack stick has equipped with spiral fan blade, the organic fertilizer fermentation and stacking can according to different height of organic fertilizer, change of different stack pole to turn effect of turning, use range is wide, use is convenient.
NOVELTY - The utility model claims a uridylic acid purifying concentrating device, a material tank, a filtering device, a ion exchange resin tank, ultra-filtration film device, wherein a material tank and filtering device through pipeline connected, the filtering device through pipeline and ion exchange resin tank connected, said ion exchange resin tank and ultra-filtration film device by pipeline connected, the ultra-filtration film device and material tank by pipeline connected, the concentration detect device fixed outside wall surface at left side of material tank middle part, a material tank bottom has material output pipe set, the ultra-filtration film bottom equipped with a waste water discharging pipe. The uridylic acid purifying device, structure is simple, can effectively obtain high concentration purification of monophosphate, increase the uridine. purifying the process efficiency, reduces the subsequent production of cost and pollute environment.
NOVELTY - Redox catalyst comprises nickel-silicon-magnesium-titanium-iron-aluminum alloy nanoparticles containing 10-40 wt.% aluminum, 50-80 wt.% iron, 0.01-2 wt.% silicon, 0.01-2 wt.% nickel, 0.01-5 wt.% titanium and 0.01-1 wt.% magnesium.    USE - The redox catalyst is useful as redox catalyst module for ultra-high wastewater processing (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) redox catalyst module comprising sheet-like structure of catalyst plate, and its arranged in 2-20 sheets;    (2) ultra-high sewage processing equipment comprising redox catalyst module; and    (3) treating wastewater using ultra-high sewage treatment equipment.
NOVELTY - Producing organic fertilizer, comprises (a) preparing a first raw material by processing organic waste, (b) preparing a functional adjuster by mixing the first raw material with the second raw material, (c) preparing a mixed raw material by mixing the first raw material with the functional adjuster, and (d) fermenting and aging the mixed raw material. The step (b) comprises (b-i) preparing a first raw material, (b-ii) preparing a second raw material, (b-iii) mixing the first raw material and the second raw material, and (b-iv) drying the mixed raw material to produce functional adjustor.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The method provides high-quality organic fertilizer, and is simple and environmentally friendly.    DETAILED DESCRIPTION - Producing organic fertilizer, comprises (a) preparing a first raw material by processing organic waste, (b) preparing a functional adjuster by mixing the first raw material with the second raw material, (c) preparing a mixed raw material by mixing the first raw material with the functional adjuster, and (d) fermenting and aging the mixed raw material. The step (b) comprises (b-i) preparing a first raw material, (b-ii) preparing a second raw material, (b-iii) mixing the first raw material and the second raw material, (b-iv) drying the mixed first and second raw material to produce the functional adjustor. The second raw material is granite soil, red clay or uncultivated soil.
NOVELTY - Converting carbon dioxide and water, comprises providing a liquid electrolyte or an electrolyte solution comprising at least one proton sponge for accumulation of carbon dioxide in the electrolyte.    USE - The method is useful for conversion of carbon dioxide and water (claimed).    ADVANTAGE - The method utilizes electrolyte (preferably 6C alcohols, ether (polyethylengylcol), amines and liquid polyamides) which cannot evaporate even for prolonged operation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) use of the proton sponge in a liquid electrolyte or an electrolyte solution, comprising conversion of carbon dioxide and water for accumulation of carbon dioxide in the electrolyte; and    (2) liquid electrolyte or electrolyte solution comprising at least one the proton sponge.
NOVELTY - Kitchen garbage aerobic fermentation device is a compact type a new type utility claims by a reaction cavity body is with stirring, cooling water circulation and the condensation water collection system, air heating and ventilation system with function of deodorization, water bath heating and heat preservation system with remote monitoring and intelligent control system is one. Inner reaction cavity body is equipped with travel switch, change electrical machine is used for stirring a; n water bath cavity is provided with heater and temperature sensor, can according to claim b. in reaction cavity body to supply heat, outside water bath cavity is a heat insulating interlayer cavity body is used for carrying out heat preservation, air heating and ventilation system a n to ensure reaction chamber comprises enough of oxygen concentration in a treatment process, cooling water circulation and the condensation water collection system can be of a water inner reaction cavity of vapour condensing derive, tail pneuma and system can prevent a malodorous gas inner reaction cavity body for a quadratic pollute environment, a PLC intelligent control by a control operation. The device structure is simple, the space use rate is high, operation energy consumption low, treatment effect is good.
NOVELTY - This utility new type is a new organic fertilizer planting machine has a fermentation pool, drying device, stirring device and a granulator, a fermentation pool a material pulverizer and material fermentation pool, a material pulverizer equipped with a protection cover has a smashing cutter, the upper part of said material pool... gas conduit has a set has a drain outlet at lower part of the drying device comprises drying a has a drying regulator, the stirring mechanism has a stirring cavity, a blanking groove, blanking opening set at the upper part of the stirring cavity, a stirring mechanism is set at the bottom of groove has more than one, the machine comprises a turntable and a material wherein, the up a pelletizer equipped with a turntable has a one or more of a material wherein set at the lower part of a machine, the new-type organic fertilizer making machine comprises a high efficiency, save a resource.
NOVELTY - This new utility model relates to a kind of one negative pressure urine collecting closeness and treatment using device, comprising gas flushing toilet system, filtering-drying system and biological high concentration fecaluria evaporation system, the gas flushing toilet system including gas flushing and vacuum pump, the filtering-drying system equipped with used for biological material to carry out filtration and biological drying treatment of organic waste filler filling the filter-biology drying device, the high concentration fecaluria evaporation system used for provided with filter liquid to carry out negative pressure evaporator and concentrated sterilization process, negative pressure evaporator generating steam used for heating the concentrated liquid and ultimately to be condensed water, filter-biology drying device discharge the solid object can as organic fertile, concentrated liquid and negative pressure evaporator discharge can as liquid organic fertile. This utility new type black product total quantity is small, the processing device relative simple structure, suitable operation, after processing the harmless and recycling high degree, to environmental influence is small, can use for each of public toilet and said toilet, sewage water and realize zero discharge and fertilizer.
NOVELTY - The device has a pan whose bottom is connected with a conveying pump. The conveying pump is connected with a pre-heater (3) through pipeline. The top of distillation tower (4) is connected to pre-heater and bottom is connected with first receiver (5). The two condensers (9,10) are provided and connected with second and third receivers (6,7). The bottom of the condenser is equipped with fourth receiver (8). The receivers are connected with a conveying pump (11) whose connecting pipe is connected to finished product tank (12,13).    USE - Device for preparing glycerol used as medicine, food, cosmetic and chemical.    ADVANTAGE - The pollution is reduced and the running cost is low.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing glycerol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for preparing glycerol.    Pre-heater (3)    Distillation tower (4)    Receivers (5,6,7,8)    Condensers (9,10)    Conveying pump (11)    Finished product tank (12,13)
NOVELTY - Producing sugar compound, comprises (a) performing physical preprocessing by crushing lignin for 100-120 minutes, and (b) saccharifying by decomposing the physically preprocessed biomass using enzyme. The physical preprocessing is carried out by crushing the mixture of biomass and buffer using ball within a container through planetary mill method or crushing the mixture of biomass and buffer using ball within the container provided with a stirrer through attrition mill method.    USE - The method is useful for producing sugar compound (claimed).    ADVANTAGE - The method maximizes energy efficiency by using lignocellulose-based biomass (claimed); minimizes cost and energy by optimizing enzyme treatment time, enzyme usage, milling time and concentration of biomass; shortens the process time; is environmentally friendly; and avoids weight loss of biomass and generation of toxic by-products.
NOVELTY - The device has a particulate matter injection unit (50) for injecting the particulate matter colliding into the film into aeration tank (30) with air injected with aeration unit (40). The aeration unit injects air colliding with the film of dipping-type membrane module (31). The membrane module performs nitrification of sewage. An anoxic chamber (10) performs de-nitrification of sewage. The anaerobic tank (20) releases phosphorus of sewage and performs solid-liquid separation of sewage by removing organic material. The aeration tank performs the organic material oxidation.    USE - Film fouling reduction-type sewage treatment device.    ADVANTAGE - Since the anaerobic tank performs solid-liquid separation of sewage by removing organic material and organic material oxidation , the film fouling is reduced and the layer washing cycle is increased. The service life time period of the film is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation method of the sewage treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of sewage treatment device.    Anoxic chamber (10)    Anaerobic tank (20)    Aeration tank (30)    Dipping type membrane module (31)    Aeration unit (40)    Particulate matter injection unit (50)
NOVELTY - One-pot synthesis of chloropyridine nitromethylene imidazolidine comprises (i) dissolving nitro-dichloro ethylene in solvent, adding sodium methylate, and ethylene diamine, and reacting, and (ii) adding catalyst, alkali, and 2-chloro-5-chloromethyl-pyridine after the reaction, collecting solid to obtain the product.    USE - The method is useful for one-pot synthesis of chloropyridine nitromethylene imidazolidine (claimed).    ADVANTAGE - The method completes all synthesis in the same reaction vessel, has high capacity utilization, has simple process and mild operation condition, can greatly reduce the three wastes, and can achieve product content of 98% after organic solvent re-crystallization.
NOVELTY - The method involves fermenting particulate biomass fiber pulp in the form of an aqueous solution of a gas-saturated aqueous gases or low boiling paraffin paraffinic compounds together with heavy paraffins with a high boiling point. Liquid paraffin-olefin blend obtained by the fermentation is distilled to temperature of 100 degrees centigrade. The obtained mixture of steam-gas is cooled and condensed to form liquefied light fuel.    USE - Method for preparation of liquid hydrocarbon fuels from biomass.
NOVELTY - Compound fertilizer comprises 45-70 pts. wt. fermented organic fertilizer, 5-15 pts. wt. urea, 10-25 pts. wt. ammonium sulfate, 8-25 pts. wt. diammonium phosphate and 7-16 pts. wt. potassium sulfate. Fermented organic fertilizer comprises 50-65 pts. wt. bagasse, 15-30 pts. wt. paddy, 8-20 pts. wt. rapeseed cake and 1-2 pts. wt. fermentation composite microbial inoculum, where water content is 10-25%.    USE - Compound fertilizer used for cultivating tea tree (claimed).    ADVANTAGE - The compound fertilizer ensures long fertilizer efficiency, reduced fertilizing time, promotes soil fertility and increased quality and yield of tea.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves:    (A) mixing bagasse, paddy, rapeseed cake and fermentation composite microbial inoculum;    (B) adjusting mixture water content to 60-70% and pH to 6.5-7.0;    (C) fermenting obtained mixture aerobically at 55?0C for 3-5 days;    (D) drying water of fermented material to 10-25% to obtain organic fertilizer;    (E) mixing organic material with urea, ammonium sulfate, diammonium phosphate and potassium sulfate; and    (F) granulating mixture to obtain product.
NOVELTY - Microbial fertilizer composition comprises 42-50 pts. wt. rock phosphate powder, 16-22 pts. wt. bran powder, 15-26 pts. wt. rapeseed cake powder, 6-12 pts. wt. urea, 1-3 pts. wt. Bacillus laterosporus and 2-4 pts. wt. B.subtilis. The rock phosphate powder comprises 15-18% phosphorus. The rock phosphate is crushed using ball mill to obtain powder having 90-100 mesh size. The bran and rapeseed cake are crushed respectively to obtain powders having 80-120 mesh size.    USE - As microbial fertilizer composition.    ADVANTAGE - The composition is convenient to use and environmentally-friendly as it causes no pollution to environment and air, changes waste into valuable resource, promotes growth of plants, and supplements nutritional components required by plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microbial fertilizer composition, which involves (a) uniformly mixing the above-mentioned components, and (b) stacking and fermenting obtained mixture, and maintaining humidity of the mixture at 30-35% during fermentation, where the air temperature is maintained at 10-20 degrees C for 20-25 minutes during stacking process or the air temperature is maintained at 20-30 degrees C for 10-15 minutes during stacking process.
NOVELTY - Preparing fertilizer involves utilizing 2-5 pts. wt. horseradish, 0.2-2 pts. wt. composite fungus, 3-6 pts. wt. Patrinia, 40-60 pts. wt. Phellodendron, 10-15 pts. wt. rapeseed, 3-7 pts. wt. silicon fertilizer, 100 pts. wt. dairy manure, 15-20 pts. wt. cow dung, 12-15 pts. wt. chicken manure, 18-30 pts. wt. pig manure, 8-12 pts. wt. plant ash, 15-22 pts. wt. willow branch and 10-18 pts. wt. canal mud. Dairy manure, chicken manure, pig manure and canal mud are dried to obtain a mixture with water content of 45-52%.    USE - Method for preparing fertilizer for protecting Salix integra disease caused by insect (claimed).    ADVANTAGE - The method enables to prepare fertilizer that improves structure and absorption efficiency of soil, and increases plant growth by providing nutrient.    DETAILED DESCRIPTION - Preparing fertilizer involves utilizing 2-5 pts. wt. horseradish, 0.2-2 pts. wt. composite fungus, 3-6 pts. wt. Patrinia, 40-60 pts. wt. Phellodendron, 10-15 pts. wt. rapeseed, 3-7 pts. wt. silicon fertilizer, 100 pts. wt. dairy manure, 15-20 pts. wt. cow dung, 12-15 pts. wt. chicken manure, 18-30 pts. wt. pig manure, 8-12 pts. wt. plant ash, 15-22 pts. wt. willow branch and 10-18 pts. wt. canal mud. Dairy manure, chicken manure, pig manure and canal mud are dried to obtain a mixture with water content of 45-52%. The mixture is crushed through a crusher into powder, and then sieved through 150 meshes to obtain granules. Granules are composting and fermenting for 35 days, and then drying to obtain fermented product with water content of 20-25%. The fermented product is crushed through 120 meshes to obtain farmyard manure. Remaining components are mixed and cultured at 15-20 degrees C for 2-3 days, and then farmyard manure is mixed to obtain fertilizer.
NOVELTY - A Micractinium inermum NLP-F014 (KCTC 12491BP) (microalgae) capable of producing biofuel, is new.    USE - The M.inermum NLP-F014 (KCTC 12491BP) (microalgae) is useful for producing biofuel (claimed).    ADVANTAGE - The microalgae is produced from biomass in concentration of 4-6 g/l, provides biomass productivity of 0.5-1 g/l/day, and lipid productivity of 0.1-0.5 g/l/day. The microalgae have higher biomass concentration and total lipid content than other existing microalgae and 16-18C fatty acids occupy most of measured lipid.
NOVELTY - Method for purifying a decarboxylated compound from plant matter, involves contacting plant matter with oil to produce an oil enriched in a carboxylic acid; and plant matter residue, separating the enriched oil and the plant matter residue, and decarboxylating the carboxylic acid in the enriched oil to produce an oil enriched in a decarboxylated compound.    USE - The method is useful for purifying a decarboxylated compound from plant matter (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for oil enriched in a decarboxylated compound.
NOVELTY - Method for preparing fertilizer involves (a) boiling beans in water, adding sugar to boiled beans, and performing aging process to obtain fermentation broth of soybean, (b) boiling spinach root in water, adding sugar to boiled spinach root, and performing aging process to obtain fermented spinach root, (c) crushing spinach leaves and stem to obtain juice, adding sugar to the juice, and performing aging process to obtain fermented spinach leaves and stem, (d) mixing the products obtained in the steps (a)-(c), and aging mixture.    USE - The method is useful for preparing fertilizer (claimed) which is used for generating folic acid in apples.    DETAILED DESCRIPTION - Method for preparing fertilizer involves (a) boiling beans in water, adding sugar to boiled beans, adding mixture into sealed vessel for fermentation process, injecting air into the mixture, and performing aging process to obtain fermentation broth of soybean, (b) boiling spinach root in water, adding sugar to boiled spinach root, adding mixture into sealed vessel for fermentation process, injecting air into the mixture, and performing aging process to obtain fermented spinach root, (c) crushing spinach leaves and stem to obtain juice, adding sugar to the juice, adding mixture into sealed vessel for fermentation process, injecting air into the mixture, and performing aging process to obtain fermented spinach leaves and stem, (d) mixing the products obtained in the steps (a)-(c), and aging mixture.
NOVELTY - A pressurizing heating jet oil-producing microorganism cell is crushed by pressing oleaginous microorganism in pipe (1) at 6-10 times speed of sound, heating pipe to 100-200 degrees C, spraying oil-producing microorganism cell to 2 blocks of parallel opposing hard side wall flat plate (2) at 15-165 degrees angle, and repeating 3-10 times.    USE - Crushing of pressurizing heating jet oil-producing microorganism cell.    ADVANTAGE - The process has high efficiency, product final temperature, cell crushing rate, and oil extraction rate, reduces transverse hole effect, unnecessary energy consumption, downstream lipid extraction, and centrifuging, is environment-friendly, does not need adding protecting agent, adjusts pH pretreatment, and saves operation time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of crushing of pressurizing heating jet oil-producing microorganism cell.    Pipe (1)    Steel plate (2)
NOVELTY - Kitchen waste is processed by performing hot alkali pretreatment and performing single-phase anaerobic fermentation.    USE - Processing of kitchen waste.    ADVANTAGE - Processing of kitchen waste is easy and increases recycling efficiency of kitchen waste.
NOVELTY - The bag has a middle clapboard (11), and a channel heat seal whose edge is formed with two cavities e.g. solid cavity and liquid cavity. The solid cavity is utilized as a solid preparation chamber, and the liquid cavity is utilized as a liquid preparation chamber. The solid preparation chamber and the liquid preparation chamber enclose a frozen excipient type supporting solvent (14) in a sealing bag (13), where the double-chamber bag is made of rubber or hot pressed aluminum-plastic composite film. The composite film is formed with an inner layer provided as a sealing layer.    USE - Frozen excipient type and supporting solvent packaging double-chamber bag for packing of food products and oral medicines.    ADVANTAGE - The double-chamber bag protects the packaged goods, and is inexpensive and easy to carry, convenient to use and environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of frozen excipient type and supporting solvent packaging double-chamber bag.    Bag body (7)    Opening end of bag body (10)    Middle clapboard (11)    Sealing bag (13)    Frozen excipient type supporting solvent (14)
NOVELTY - Method for adsorbing oil in kitchen wastewater by processing straw, involves crushing the straw, adding flocculant, mixing, adding the mixture into the kitchen wastewater, adsorbing organic matter, separating and collecting oil.    USE - The method is used for adsorbing oil in kitchen wastewater using straw (claimed).    ADVANTAGE - The method is cost-effective.
NOVELTY - Low-temperature purification of second alkali mother liquid includes attaching insoluble object on backwashing ceramic microfilter film component, mixing generated backwash waste liquid with thickener into soda production process of ammonium process, settling, taking thick material for the preparation of agricultural ammonium chloride, taking backwash waste supernatant liquid, mixing with thick liquid overflow, returning to ammonium process liquor system, settling, taking thick material for agricultural ammonium chloride, and mixing clear liquid in waste liquid overflow with thickener.    USE - Method for low-temperature purification of second alkali mother liquid used as fertilizer (claimed).    ADVANTAGE - The liquid has low ammonium, calcium, and magnesium levels as to not affect its use as a fertilizer. The method achieves recycling of heat, and zero emission of wastewater and solid waste.    DETAILED DESCRIPTION - Low-temperature purification of second alkali mother liquid comprises attaching insoluble object on backwashing ceramic micro-filter film component, mixing generated backwash waste liquid with thickener into soda production process of ammonium process, settling, taking thick material for the preparation of agricultural ammonium chloride, taking backwash waste supernatant liquid, mixing with thick liquid overflow, returning to ammonium process liquor system, settling, taking thick material for agricultural ammonium chloride, mixing clear liquid in waste liquid overflow with thickener, returning to mother liquid system in ammonium process, filtering with ceramic microfilter film attached on heat exchanger, absorbing second mother liquid to produce calcium, magnesium, and sand, and using backwash waste liquid in production process of ceramic microfilter film to carry out reverse flushing.
NOVELTY - Fermentation agent comprises 7x 107-7.5x 107 colony-forming unit (CFU)/g Bacillus firmus, 4x 107-5x 107 CFU/g Bacillus subtilis, 3x 107-4x 107 Bacillus coagulans, 300-350 enzyme unit (U)/g acidic protease, 200-250 U/g xylanase, 200-250 U/g cellulase, 0.4-0.45 wt.% sodium citrate trisodium salt dihydrate and 0.2-0.3 wt.% ammonium iron (II) sulfate hexahydrate.    USE - Fermentation agent used for reducing cow dung ammonium nitrogen content (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of fermentation agent comprising inoculating raw materials with cassava residue and cow manure and performing anaerobic fermentation at room temperature.
NOVELTY - Fermenting organic fertilizer comprises e.g. mixing excrement, straw, sawdust, mushroom residue and clay powder, diluting and uniformly spreading the material and stacking, carrying out fermentation, maintaining the moisture of fermentation material, in intermediate temperature, microorganism are active, continuously increasing the stack temperature, quickly decomposing organic matter, continuing to break down organic matter, gradually decomposing part of cellulose and lignin, and forming humus, curing after completing fermentation, and refining finished product organic fertilizer.    USE - The method is useful for fermenting organic fertilizer (claimed).    ADVANTAGE - The fertilizer is safe, easy to use, has resistance to disease, and promotes fertility.    DETAILED DESCRIPTION - Fermenting organic fertilizer comprises (i) raw material processing: mixing excrement, straw, sawdust, mushroom residue and clay powder, diluting and uniformly spreading the material and stacking, and carrying out mixed fermentation, (ii) fermenting: maintaining the moisture of fermentation material to be at 60-65%, when the temperature is 25-45 degrees C, in intermediate temperature, microorganism are active, continuously increasing the stack temperature, when the temperature is 45-65 degrees C, the high temperature thermophilic microorganism, and actinomycete gradually occupy predominantly, in intermediate temperature microorganism restrains or even cause death, more quickly decomposing organic matter, making stack temperature quickly increase to 60-70 degrees C, at this time, continuing to break down organic matter and decomposing outside, gradually decomposing part of cellulose and lignin, and forming humus, and (iii) curing: after completing fermentation process for 5-7 days, refining finished product organic fertilizer as bulk, which is brown, slightly with wine aroma or earthy flavor.
NOVELTY - Preparation of antimicrobial growth promoting agent involves dissolving chitosan in acetic acid solution, heating, stirring, adding hydrogen peroxide solution, obtaining chitosan solution, emulsifying, adding mixture of Bacillus subtilis, Bacillus megaterium and Bacillus laterosporus, mixing, adding biogas slurry, fermenting at 25-30 degrees C for 10-20 hours, obtaining chitosan fermentation agent, adding rare-earth compound and bamboo vinegar liquid, and mixing.    USE - Preparation of antimicrobial agent used for promoting growth of vegetables.    ADVANTAGE - The method enables preparation of nutritious, environmentally-friendly and non-toxic antimicrobial growth promoting agent with high yield.
NOVELTY - Generating powder involves fermenting garbage by using microorganism to obtain obtained fermentation product. The fermentation product is desulfurized, carbon dioxide is removed and then dehydrated to obtain biomass gas. The powder is generated by gas turbine using biomass gas and heat is provided for performing fermentation by gas turbine. Cooling water is utilized for garbage microbial fermentation.    USE - Method for generating powder (claimed).    ADVANTAGE - The method enables to generate power with zero emission waste, and reduces energy consumption and environmental pollution and increases utilization of new energy sources.
NOVELTY - The processor has a bracket fixed with a motor that is fixed with a drive shaft through a speed reducer. The drive shaft is fixed with a driven roller wheel that is fixed with a connecting support. A storage bin is fixed with the bracket that is fixed with a supporting roller wheel. A front end of a storage hopper is fixed with the storage bin. A rotating joint is fixed with a rear end of the storage bin and a gas/water pipe that is fixed with an air inlet pipe and a discharge pipe. A front end of the rotating joint is fixed with a front cone section of the storage bin.    USE - Rotary kitchen waste biochemical processor.    ADVANTAGE - The processor can realize the kitchen waste feeding and discharging function, and has low power consumption and high processing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a rotary kitchen waste biochemical processor.
NOVELTY - This utility new type relates to a planting fertilizer production device, specifically is a ammoniation granulating a thio base compound fertilizer with potassium hydrogen production reaction groove. Comprising a shell, set up at upper end is provided with a stirring shaft inner shell and fixed mounting of a stirring shaft upper blade, a shell inner wall has equipped with heating pipe, shell is interlayer wall ring groove, lower end set with lower ring groove, a heating pipe set with lengthways, two upper heating tube is a connected ring groove and a lower ring groove, a ring groove side wall is set with connected air inlet hole of inner cavity shell and connected absorption liquid conveying mechanism of liquid inlet pipe, lower ring groove is a side wall set with connected liquid absorption mechanism is a liquid outlet pipe. This reaction groove structure is reasonable, tail pneuma absorption fully, using tail pneuma absorption process in a heat energy of heating reaction groove, compact structure, low energy consumption.
NOVELTY - A wet product mix of clofentezine is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation-dehydrated in film evaporator, dehydrated, wet-ground, modulated, and packaged for continuous operation. Solution of mancozeb, zinc complex and organic solvent is added to mixture, and dehydration-crystal-transformed, to obtain clofentezine.    USE - Preparation of clofentezine (claimed).    ADVANTAGE - The method enables preparation of clofentezine, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparing polyoxin comprises (a) taking organic solvent and polyoxin wet product, distilling and dehydrating, (b) taking solvent as a carrier, injection heating or through film evaporator, distilling and dehydrating, wet grinding, modulating, packaging, continuously operating and (c) adding mancozeb and zinc simultaneously into the crystal complex, dehydrating and transforming crystal in the organic solvent.    USE - The method is useful for preparing polyoxin (claimed).    ADVANTAGE - The method: reduces the pollution of harmful impurities and dust; reduces decomposition of the products; and avoids fire accidents during product drying process.
NOVELTY - Preparing dichlorobenzene comprises (i) mixing organic solvent and wet product of dichlorobenzene, distilling, and dehydrating; and (ii) taking the solvent as carrier, subjecting to injection heating process or heating, distilling, and dehydrating through a film evaporator to enable the dehydration process and wet smashing process, modulating, packaging, and continuously operating.    USE - The method is useful for preparing dichlorobenzene (claimed).    ADVANTAGE - The method: reduces the decomposition products, reduces harmful impurities and dust pollution; and avoids the occurrence of fire accident during product drying process.
NOVELTY - Preparing heptachlor comprises: (a) adding an organic solvent into distilled-dehydrated heptachlor wet product; (b) carrying out distillation and dehydration via injection heating or film evaporator, carrying out wet grinding, modulating and packaging for continuous operation; and (c) adding mancozeb and zinc organic solvent complex and dehydrating to crystallize.    USE - The method is useful for preparing heptachlor (claimed).    ADVANTAGE - The method avoids the pollution of harmful impurities and dust.
NOVELTY - A wet product mix of triazolone is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation-dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain triazolone.    USE - Preparation of triazolone (claimed).    ADVANTAGE - The method enables preparation of triazolone, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - A wet product mix of carbosulfun is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complexes and an organic solvent is added to mixture and the mixture is dehydration-crystal transformed, to obtain carbosulfun.    USE - Preparation of carbosulfun (claimed).    ADVANTAGE - The method enables preparation of carbosulfun, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Processing hexythiazox comprises (i) mixing an organic solvent used in preparing hexythiazox and hexythiazox wet product, distilling and dehydrating; (ii) heating or heating, distilling and dehydrating through a film evaporator, wet grinding, modulating and packaging; and (iii) complexing in maneb and zinc containing organic solvent, dehydrating and carrying out crystal transformation.    USE - The method is useful for processing hexythiazox (claimed).    ADVANTAGE - The method reduces decomposing of product, avoids fire accident in drying process and reduces generation of harmful impurities and dust.
NOVELTY - A wet product mix of iminoctadine is distillation-dehydrated using organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complexes and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain iminoctadine.    USE - Preparation of iminoctadine (claimed).    ADVANTAGE - The method enables preparation of iminoctadine, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - A wet product mix of fenpropathrin is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and organic solvent is dehydration-crystal transformed, to obtain fenpropathrin.    USE - Preparation of fenpropathrin (claimed).    ADVANTAGE - The method enables preparation of fenpropathrin, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparing fenbutatin oxide complex involves dehydrating fenbutatin oxide using organic solvent, where solvent as the carrier is injected through heating or film evaporator distillation process. The dehydrated product is complexed with mancozeb and zinc to obtain product that is crushed, wet ground, modulated and packaged.    USE - Method for preparing fenbutatin oxide complex (claimed).    ADVANTAGE - The method enables to prepare fenbutatin oxide complex that ensures reduced decomposition, pollution and generation of harmful impurity and dust, and requires no product drying process to save from fire accident generation.
NOVELTY - Preparing heptenophos involves mixing phosphorus with organic solvent and performing distillation process. The mixture is dehydrated by heating in evaporator and then carrying out wet grinding process to obtain powder. Mancozeb is mixed with powder and then zinc is added to form zinc complex. Zinc complex is subjected to crystal transformation process to obtain final product.    USE - Method for preparing heptenophos (claimed).    ADVANTAGE - The method enables to prepare heptenophos in an eco-friendly manner.
NOVELTY - Preparing coumaphos complex involves dehydrating coumaphos using organic solvent, where solvent as the carrier is injected through heating or film evaporator distillation process. The dehydrated product is complexed with mancozeb and zinc using organic solvent to obtain product that is crushed, wet ground, modulated and packaged.    USE - Method for preparing coumaphos complex (claimed).    ADVANTAGE - The method enables to prepare coumaphos complex that ensures reduced decomposition, pollution and generation of harmful impurity and dust, and requires no product drying process to save from fire accident generation.
NOVELTY - A wet product mix containing Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate) is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is dehydration-crystal transformed, to obtain Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate).    USE - Preparation of Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate) (claimed).    ADVANTAGE - The method enables preparation of Dipterex (RTM: dimethyl-(2,2,2-trichloro-1-hydroxyethyl) phosphonate), with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - A wet product mix containing aluminum phosphide is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complex and an organic solvent is added to mixture, and the mixture is dehydration-crystal transformed, to obtain aluminum phosphide.    USE - Preparation of aluminum phosphide (claimed).    ADVANTAGE - The method enables preparation of aluminum phosphide, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparing pyrethrin comprises: (a) adding an organic solvent into distilled-dehydrated pyrethrin wet product; (b) carrying out distillation and dehydration via injection heating or film evaporator, carrying out wet grinding, modulating and packaging for continuous operation; and (c) adding mancozeb and zinc organic solvent complex and dehydrating to crystallize.    USE - The method is useful for preparing pyrethrin (claimed).    ADVANTAGE - The method avoids the pollution of harmful impurities and dust.
NOVELTY - Preparation of rivaroxaban (I) involves reacting benzyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate (II) and (2R)-1-chloro-3-((E)-((4-chlorophenyl)methylidene)amino)propan-2-ol (III) in an organic solvent (s1), obtaining 4-(4-((5R)-5-(((E)-((4-chlorophenyl)methylidene)amino)methyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (IV), hydrolyzing, obtaining 4-(4-((5R)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one (V), extracting using organic solvent (s2), removing organic phase, adding inorganic base and 5-chloro-thiophene chloride (VI) to aqueous phase, and reacting.    USE - Preparation of rivaroxaban (claimed).    ADVANTAGE - The method enables simple, environmentally-friendly and economical preparation of rivaroxaban with less number of steps.    DETAILED DESCRIPTION - Preparation of rivaroxaban of formula (I) involves reacting benzyl N-(4-(3-oxomorpholin-4-yl)phenyl)carbamate of formula (II) and (2R)-1-chloro-3-((E)-((4-chlorophenyl)methylidene)amino)propan-2-ol of formula (III) in an organic solvent (s1) in presence of lithium tert-butoxide, obtaining 4-(4-((5R)-5-(((E)-((4-chlorophenyl)methylidene)amino)methyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one of formula (IV), hydrolyzing the resultant product using hydrochloric acid, obtaining 4-(4-((5R)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one of formula (V), extracting the resultant product using organic solvent (s2), removing organic phase, adding inorganic base and 5-chloro-thiophene chloride of formula (VI) to the aqueous phase, and reacting.
NOVELTY - Composition consists of: a particulate organic material having a water content of less than 30 wt.%; hydrogel; and fertilizer agent. The fertilizer agent contains processed sludge with organic materials and active microorganisms.    USE - The composition is useful for supporting and accelerating the processes of composting. No biological data given.
NOVELTY - Preparation of trimethobenzamide hydrochloride (I) involves reacting (process A) 4-hydroxybenzaldehyde with 2-(dimethylamino)ethyl chloride in organic solvent (a) and inorganic base, treating (process B) obtained 4-(dimethylaminoethoxy)benzaldehyde with raney nickel in methanolic ammonia, and coupling (process C) with N-(3,4,5-trimethoxybenzoyl)imidazole (VI) in presence of organic solvent, quenching with water and concentrating the organic layer, and treating (process D) with paraformaldehyde and formic acid in organic solvent (d) and separating trimethobenzamide hydrochloride.    USE - Preparation of trimethobenzamide hydrochloride used as agent for treating nausea associated with gastrointestinal disturbances and motion sickness or nausea induced by administering therapeutic agent.    ADVANTAGE - The method enables economical and environmentally-friendly preparation of trimethobenzamide hydrochloride with high purity and yield without performing column chromatography or other purification methods.    DETAILED DESCRIPTION - Preparation of trimethobenzamide hydrochloride of formula (I) involves reacting (process A) 4-hydroxybenzaldehyde with 2-(dimethylamino)ethyl chloride in organic solvent (a), inorganic base, quenching reaction mixture with aqueous inorganic acid, extracting with ethyl acetate with pH of 8-9, and separating 4-(dimethylaminoethoxy)benzaldehyde, treating (process B) 4-(dimethylaminoethoxy)benzaldehyde with raney nickel in methanolic ammonia, coupling (process C) 4-(dimethylaminoethoxy)benzylamine with N-(3,4,5-trimethoxybenzoyl)imidazole of formula (VI) in presence of inorganic base and organic solvent, quenching with water and concentrating the organic layer, and treating (process D) with paraformaldehyde and formic acid in organic solvent (d) and separating trimethobenzamide hydrochloride.
NOVELTY - The system has a stationary baffle for dividing tide generation units into compartments (1-6) that include independent volume, where flow pattern of upward and downward directions is maintained for the tide generation units. The tide generation units are filled with aggregate of different size for filtration of wastewater. One of partition coffers (7) provides facility to generate tides. A trapezoidal trough comprises inclination of 65 degrees that is provided at center of a horizontal wetland unit (10), where marshy soil is filled in the trough upto 0.08 meters.    USE - Artificial wetland system for facilitating treatment of domestic waste water using green bulrush plants.    ADVANTAGE - The system allows tides to be generated of minimum thickness so as to enhance introduction of oxygen from atmosphere in an efficient manner. The system facilitates treatment of domestic waste water using plants to remove pollutants from the water in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of artificial wetland system.    Compartments (1-6)    Partition coffers (7, 8, 9)    Horizontal wetland unit (10)    Inlet (11)    Outlet (12)
NOVELTY - The composite bacteria AH/O biological deep purification and micro power cycle processing method involves: (a) using raw river water for a period of 7-10 days of acclimatization of bacteria, importing amplification within the filling and mixing with nutrients; (b) developing bacteria in amplification tanks (I) and (II), where tank (I) contains group (A) bacteria bed, and tank (II) contains group (B) bacteria bed; (c) passing the sewage through grid, and then introducing into group (A) bacteria bed and anaerobically treating sewage.    USE - Composite bacteria AH/O biological purification and micro power cycle processing method of sewage (claimed).    ADVANTAGE - The method enables simple, effective, stable, reliable and convenient processing and maintenance of sewage.    DETAILED DESCRIPTION - The composite bacteria AH/O biological deep purification and micro power cycle processing method involves: (a) using raw river water for a period of 7-10 days of acclimatization of bacteria, importing amplification within the filling and mixing with nutrients; (b) developing bacteria in amplification tanks (I) and (II), where tank (I) contains group (A) bacteria bed, and tank (II) contains group (B) bacteria bed and connecting the (A) and (B) strains of bacteria bed in series; (c) passing the sewage through grid, and then introducing into group (A) bacteria bed and anaerobically treating sewage; and (d) introducing anaerobically treated sewage into group (B) bacteria bed, and then oxidizing.
NOVELTY - The processor comprises stirring shaft (2) mounted inside stirring tank (1) and fixedly connected with both ends of stirring tank. The vanes (3) are fixed to end of stirring shaft. The vanes from long to short lengths and from short to long gradients, are uniformly distributed over the circumference of the stirring shaft.    USE - Biodegradable processor of livestock manure.    ADVANTAGE - Livestock manure is contacted with composite functional bacteria, thus ensuring sufficient contact with oxygen and bacteria. The breeding of composite functional bacteria is enabled by contact of composite functional bacteria with oxygen. The degradation rate of livestock manure is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of biodegradable processor of livestock manure.    Stirring tank (1)    Stirring shaft (2)    Vanes (3)    Reinforcing rib (4)
NOVELTY - The system has fermentation tunnel (7), shutter door (10), fan (1), heater (2), air inlet pipes (4,5), air distribution pipe (8), air outlet (11), fermentation cage (6), and winch (3). The fermentation channel is provided with two shutter doors. Both ends of the shutter doors are connected at bottom of wall outlet of fermentation tunnel. The fan is connected with heater. The air inlet pipe is connected to air distribution pipe.    USE - Continuous fermentation apparatus for solid such as livestock manure, crop straw, and domestic solid waste.    ADVANTAGE - The uniform fermentation, stable fermentation quality, low energy consumption, low operation cost and continuous treatment of solid fermentation apparatus are ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous domestic waste solid fermentation apparatus.    Fan (1)    Heater (2)    Winch (3)    Air inlet pipes (4,5)    Fermentation cage (6)    Fermentation tunnel (7)    Air distribution pipe (8)    Shutter door (10)    Air outlet (11)
NOVELTY - A pesticide with isocyanate as intermediate is prepared by preparing amine solution in which ratio of amine and solvent is 1:2-8 at 20-40 degrees C, stirring amine solution and phosgene in 1:3-8 in cold light kettle in which ratio of amine and solvent is 1:5-20, reacting for 3-5 hours at 10-20 degrees C, carrying out photochemical reaction of isocyanate solution, carrying out light chemical reaction at 801-40 degrees C and 0-1 bar for 4-6 hours, and carrying out cold light chemical reaction and light chemical reaction separation of hydrochloric acid and unreacted phosgene through condenser.    USE - Preparation of pesticide with isocyanate as intermediate (claimed).    ADVANTAGE - Raw material is easy to obtain, costs low and has small by-product. Pesticide product concentration is stable and environmentally friendly.    DETAILED DESCRIPTION - A pesticide with isocyanate as intermediate is prepared by preparing amine solution in which ratio of amine and solvent is 1:2-8 at 20-40 degrees C, stirring amine solution and phosgene in 1:3-8 in cold light kettle in which ratio of amine and solvent is 1:5-20, reacting for 3-5 hours at 10-20 degrees C, carrying out photochemical reaction of isocyanate solution, carrying out light chemical reaction at 801-40 degrees C and 0-1 bar for 4-6 hours, carrying out cold light chemical reaction and light chemical reaction separation of hydrochloric acid and unreacted phosgene through condenser, removing phosgene in phosgene absorption tower by solvent in which isocyanate concentration is 10-30 wt.%, separating pesticide product and removing solvent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the preparation of pesticide. (Drawing includes non-English language text).
NOVELTY - Synthesis of substituted indole-2-carboxylic acid involves performing 1st step of adding phenylhydrazine or substituted phenylhydrazine hydrochloride and ethyl pyruvate in solvent, refluxing at 50-80 degrees C, monitoring reaction for 3-5 hours, removing solvent, recrystallizing with aqueous ethanol, filtering, and obtaining substituted phenylhydrazone as pale yellow crystal, and performing 2nd step of stirring mixture of polyphosphoric acid and phosphoric acid, heating at 50-110 degrees C, and adding substituted phenylhydrazone in portions for 0.5-1.5 hour.    USE - Synthesis of substituted indole-2-carboxylic acid (claimed).    ADVANTAGE - The process is simple and environmentally friendly, generates small amount of waste, and produces indole-2-carboxylic acid with high purity in high yield.    DETAILED DESCRIPTION - Synthesis of substituted indole-2-carboxylic acid involves performing 1st step of adding phenylhydrazine or substituted phenylhydrazine hydrochloride and ethyl pyruvate in solvent, refluxing at 50-80 degrees C, monitoring reaction for 3-5 hours, removing solvent, recrystallizing with aqueous ethanol, filtering, and obtaining substituted phenylhydrazone as pale yellow crystal, performing 2nd step of stirring mixture of polyphosphoric acid and phosphoric acid, heating at 50-110 degrees C, adding substituted phenylhydrazone in portions for 0.5-1.5 hour, controlling temperature to 70-120 degrees C, reacting for 10-40 minutes, pouring into ice water mixture, cooling, filtering, drying, and obtaining substituted indole-2-carboxylic acid ethyl ester as pale yellow solid product, and performing 3rd step of heating and refluxing sodium hydroxide solution and substituted indole-2-carboxylic acid ethyl ester for 0.5-1 hour, cooling at 20-60 degrees C, adding hydrochloric acid to adjust pH to 3-4, cooling, drying, and obtaining product.
NOVELTY - Preparing 1-(4-isothiocyanatophenoxy)-4-nitrobenzene (I) comprises: (a) condensing 1-chloro-4-nitrobenzene (V) with N-(4-hydroxyphenyl)acetamide (VI) in presence of a base and solvent to give N-(4-(4-nitrophenoxy)phenyl)acetamide (IV); (b) hydrolyzing (IV) in presence of an acid in a solvent to give 4-(4-nitrophenoxy)aniline hydrochloride (III); (c) reacting (III) with ammonium thiocyanate in presence of a solvent to obtain 1-(4-(4-nitrophenoxy)phenyl)thiourea (II); and (d) deaminating (II) using base in presence of a solvent to give (I).    USE - The process is useful for preparing (I) (claimed), which is used as anthelmintic drug. No biological data given.    ADVANTAGE - The process avoids the use of hazardous, teratogenic and mutagenic reagents, and reduces the reaction time, thus providing (I) in an economical manner.    DETAILED DESCRIPTION - Preparing 1-(4-isothiocyanatophenoxy)-4-nitrobenzene of formula (I) comprises: (a) condensing 1-chloro-4-nitrobenzene of formula (V) with N-(4-hydroxyphenyl)acetamide of formula (VI) in presence of a base and solvent to give N-(4-(4-nitrophenoxy)phenyl)acetamide of formula (IV); (b) hydrolyzing (IV) in presence of an acid in a solvent to give 4-(4-nitrophenoxy)aniline hydrochloride of formula (III); (c) reacting (III) with ammonium thiocyanate in presence of a solvent to obtain 1-(4-(4-nitrophenoxy)phenyl)thiourea of formula (II); and (d) deaminating (II) using base in presence of a solvent to give (I).
NOVELTY - 2-Cyclohexen-1-one (VI) is condensed with diethyl methylmalonate (VII) using reagent in presence of solvent (a) without distillation, to obtain dimethyl methyl(3-oxocyclohexyl)malonate (IV). Compound (IV) is reacted with (4-chlorophenyl)hydrazine (V) or its hydrochloride salt, to form dimethyl (6-chloro-2,3,4,9-tetrahydro-1H-carbazol-2-yl)methylmalonate (III). Compound (III) is dehydrogenated using chloranil, to obtain dimethyl (6-chloro-9H-carbazol-2-yl)methylmalonate (II). Compound (II) is hydrolyzed and decarboxylated, to obtain 2-(6-chloro-9H-carbazol-2-yl)propanoic acid (I).    USE - Preparation of 2-(6-chloro-9H-carbazol-2-yl)propanoic acid used as non-steroidal drug for treating inflammation, osteoarthritis, hip dysplasia and arthritis, and relieving joint pain.    ADVANTAGE - The 2-(6-chloro-9H-carbazol-2-yl)propanoic acid is prepared without carrying out distillation, and without using carcinogenic benzene and hazardous class-1 solvent.    DETAILED DESCRIPTION - 2-Cyclohexen-1-one of formula (VI) is condensed with diethyl methylmalonate of formula (VII) using reagent in presence of solvent (a) without distillation, to obtain dimethyl methyl(3-oxocyclohexyl)malonate of formula (IV). Compound (IV) is reacted with (4-chlorophenyl)hydrazine of formula (V) or its hydrochloride salt in presence of solvent (b), to form dimethyl (6-chloro-2,3,4,9-tetrahydro-1H-carbazol-2-yl)methylmalonate of formula (III). Compound (III) is dehydrogenated using chloranil in presence of solvent (c), to obtain dimethyl (6-chloro-9H-carbazol-2-yl)methylmalonate of formula (II). Compound (II) is hydrolyzed and decarboxylated using acid (A), to obtain 2-(6-chloro-9H-carbazol-2-yl)propanoic acid of formula (I).
NOVELTY - The second medicine adding. This utility new type claims a farm solid waste and a resource using a sewage, comprising sewage treatment system, sewage processing system comprises orderly connected a biochemical process pool, the pH regulating pool, the reaction pool, precipitating pool and concentrated pool, the pH regulating pool inside has regulating a dosing system, the reaction pool sewage pH value of inner is equipped with a sewage in adding Mg2 + and PO43-is, further comprising a solid precipitate and farm solid waste of pool. carry out compost treatment of compost. Through install precipitation pool, adding Mg2 to sewage + and PO43-to the ammonia nitrogen in sewage of precipitate, at the same time and matching a compost farm solid waste treatment for ammonia nitrogen conversion into fertilizer, which not only can make the water ammonia nitrogen reaches the standard, and the resource a circulation use, it is very accord with construction resource saving type, claim of environment-friendly type. At the same time, a certain of economic benefit, a solid precipitate and farm solid waste with a compost treatment, can greatly increase fertilizer effect.
NOVELTY - A micronutrient fertilizer component preparing method involves utilizing biomass selected from micro-algae, spirulina, berries, kernels and mushroom substrate. Carboxyl, hydroxyl or phosphoryl functional groups existed on a surface of cell walls of the biomass are bound with trace elements such as 3.0-12.0 mg/g manganese, 5.0-35.0 mg/g zinc and 12-40 mg/g copper. Ion-exchanged process is carried out on aqueous solutions of manganese sulfate and the trace elements to obtain a finished product.    USE - Method for preparing micronutrient fertilizer components.    ADVANTAGE - The method enables improving growth of plant in an effective manner.
NOVELTY - Preparation of rosuvastatin side chain intermediate involves adding aqueous buffer to a reactor, adding a portion of 6-chloro-3,5-dicarbonyl-tert-butyl hexanoate, isopropanol and biocatalyst, stirring, adding another portion of 6-chloro-3,5-dicarbonyl-tert-butyl hexanoate when the reaction conversion rate is 80-100%, reacting resultant mixture, adding ethyl acetate to the reaction mixture, extracting several times, combining organic phases, evaporating to remove solvent, and obtaining (3R,5S)-6-chloro-3,5-dihydroxy-tert-butyl hexanoate.    USE - Preparation of rosuvastatin side chain intermediate by dual enzymatic method (claimed).    ADVANTAGE - The method enables economical preparation of rosuvastatin side chain intermediate with reduced energy consumption, by simple process.    DETAILED DESCRIPTION - Preparation of rosuvastatin side chain intermediate involves adding aqueous buffer to a reactor, adding a portion of 6-chloro-3,5-dicarbonyl-tert-butyl hexanoate, isopropanol and biocatalyst, stirring at 25-40 degrees C, detecting the reaction process by gas chromatography, adding another portion of 6-chloro-3,5-dicarbonyl-tert-butyl hexanoate when the reaction conversion rate is 80-100%, reacting resultant mixture, completing the reaction when the reaction conversion rate is 95-100%, adding ethyl acetate to the reaction mixture, extracting several times, combining organic phases, evaporating to remove solvent, and obtaining (3R,5S)-6-chloro-3,5-dihydroxy-tert-butyl hexanoate.
NOVELTY - Bacillus halodurans ANU101 strain (KACC91847P) having lipase activity and antibiotic resistance to ampicillin, kanamycin, tetracycline and streptomycin, is new.    USE - The strain is useful as microbial agent for decomposing waste food, producing feed additive composition (all claimed), and killing pathogenic microorganisms.    ADVANTAGE - The strain improves nutrients, carbohydrate, fiber and protein in food.
NOVELTY - New fatty acid produced from Artemisia annua oil has acid value of 130-150 mg potassium hydroxide/g, free fatty acid content of 60-70%, saponification value of 150-170 mg potassium hydroxide/g, iodine value of 45-55 mg/100 g, saturated fatty acid relative content of 32-36%, monounsaturated fatty acid relative content of 7-9%, and polyunsaturated fatty acid relative content of 5-6%.    USE - The fatty acid is used as raw material for preparing drug and food products (all claimed).    ADVANTAGE - The environmentally-friendly and healthcare fatty acid has excellent physiological activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation the fatty acid, which involves using Artemisia annua oil, petroleum ether, sodium hydroxide, methanol, 0.2-0.8 mol/L hydrochloric acid, and diethyl ether.
NOVELTY - Bioorganic fertilizer comprises 18 pts. wt. chicken manure, 12 pts. wt. maggot, 2 pts. wt. ammonium molybdate, 0.8 pt. wt. fermentation strain, 25 pts. wt. plant ash, 8 pt. wt. soyabean pulp, 12 pts. wt. corn straw, and 18 pts. wt. mud.    USE - The bioorganic fertilizer is useful for growing vegetables and grape.    ADVANTAGE - The fertilizer utilizes waste, and has balanced nutrition.
NOVELTY - Method for preparing bio-organic fertilizer involves crushing wheat straw, spraying microbial inoculum on crushed wheat straw, where moisture content of sprayed mixture is 70-85%, where the microbial inoculum comprises Trichoderma viride, T.aureoviride, and Paenibacillus in a mass ratio of 1:0.9-1.5-1-1.8.    USE - The method is useful for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare product within short period of time. The prepared product is nontoxic, rich in nutrients, environmentally-friendly and increases quality of crops.
NOVELTY - Method for aerobic composting of livestock manure involves collecting straw, livestock manure and compost powder, measuring total carbon, total nitrogen, carbon to nitrogen ratio and water contents, mixing above-mentioned raw materials, adding 7-20 %mass humus soil, maintaining 65-70% moisture content, fermenting mixture for 1-4 days, composting fermented mixture for 16-35 days, simultaneously mixing once every 7 days during composting, measuring total organic carbon, total organic nitrogen and total humic acid contents, and determining the quality of the compost.    USE - The method is useful for aerobic composting of livestock manure by adding humus soil (claimed).    ADVANTAGE - The method enables to produce livestock manure compost with improved quality.    DETAILED DESCRIPTION - Method for aerobic composting of livestock manure by adding humus soil, involves (a) collecting straw, livestock manure and compost powder, measuring total carbon, total nitrogen, carbon to nitrogen ratio and water contents, mixing above-mentioned raw materials, adding 7-20 %mass humus soil and maintaining 65-70% moisture content, where the straw and livestock manure are in mass ratio of 25-30:1, (b) fermenting mixture for 1-4 days under open condition, then composting fermented mixture for 16-35 days, and simultaneously mixing once every 7 days during composting, and (c) measuring total organic carbon, total organic nitrogen and total humic acid contents, and determining the quality of the compost.
NOVELTY - Diazepam intermediate i.e. N-methyl-3-phenyl-5-chloro-2,1-benzisoxazolium methyl carbonate (I) is new.    USE - Used as diazepam intermediate i.e. N-methyl-3-phenyl-5-chloro-2,1-benzisoxazolium methyl carbonate.    ADVANTAGE - The preparation method: is simple; utilizes less harmful/toxic reagents; has simple product isolation and purification steps, and low equipment corrosion; and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Diazepam intermediate i.e. N-methyl-3-phenyl-5-chloro-2,1-benzisoxazolium methyl carbonate of formula (I) is new. An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Hydrocortisone butyrate is recovered from hydrocortisone mother liquid by refining hydrocortisone, separating filter liquid, concentrating, evaporating organic solvent to obtain viscous material, adding methanol, continuously decompression-concentrating, adding mixed solvent, continuously stirring, dropwise adding methyl alcohol in alkali solution under inert gas protection, continuously heat preserving to complete reaction, dropwise adding methyl alcohol in acidic solution to neutralize pH, decompression-concentrating, adding elution agent, freezing, filtering and drying.    USE - Recovery of hydrocortisone butyrate from hydrocortisone mother liquid (claimed).    ADVANTAGE - The process has feasible operation, short process, low cost, and high production safety, material stability, and recovery rate, does not cause pollution, and obtains high purity product.    DETAILED DESCRIPTION - Hydrocortisone butyrate is recovered from hydrocortisone mother liquid by refining hydrocortisone, separating filter liquid, concentrating, evaporating organic solvent to obtain viscous material which is hydrocortisone butyrate mother liquid containing 65% hydrocortisone, adding methanol, continuously decompression-concentrating until viscous, adding mixed solvent, continuously stirring to dissolve, dropwise adding methyl alcohol in alkali solution under inert gas protection, continuously heat preserving to complete reaction, dropwise adding methyl alcohol in acidic solution to neutralize pH to 6-7, decompression-concentrating until thick, adding elution agent, freezing, filtering, and drying.
NOVELTY - Invention relates to methods of producing hydrogen by hydrolysis of a solid reagent - aluminium - in a reaction vessel and can be used to produce hydrogen in stand-alone power generation, primarily in power plants with electrochemical generators, such as fixed plants, on vehicles, and when repairing hydrogen-cooled electric generators and in chemical industry. Disclosed is a method of producing hydrogen by hydrolysis of aluminium in a reaction vessel filled with aqueous sodium hydroxide solution. The method of producing hydrogen is carried out in a continuous reactor by feeding aluminium in the form of an aqueous suspension. Before feeding into the reaction vessel, the aqueous suspension of aluminium is gelled (thickened). The gelling (thickening) additive used is modified polyacrylic acid or agar-agar.    USE - Chemistry.    ADVANTAGE - Invention increases cost effectiveness of producing hydrogen and improves the quality of hydrolysis and control of the hydrogen production process.2 cl, 2 dwg
NOVELTY - Preparing methane from materials having different amounts of carbon, comprises: incubating microorganisms of consortium TPM3 isolated from peat soils, on nutrient medium enriched with vitamins, trace elements and antibiotics under anaerobic conditions at 10-30 degrees C and light; inoculating materials containing more than 6% organic carbon with the resulting culture of microorganisms; and incubating to allow the occurrence of methanogenesis, where the initiation of the conversion of carbon takes place under anaerobic conditions in an atmosphere containing carbon dioxide of 0.1-50% under nitrogen.    USE - The process is useful for preparing methane from materials having different amounts of carbon.
NOVELTY - A Scenedesmus quadricauda strain SDEC-8 (CCTCC M 2014448), is new.    USE - The S.quadricauda strain SDEC-8 is useful for processing eutrophic lakes, purifying nitrogen and phosphorus containing wastewater, and producing high-fat, fatty acid, protein, starch, pigment, polysaccharide, nucleic acid (all claimed) and biodiesel.    ADVANTAGE - The S.quadricauda strain SDEC-8 has excellent oxidation stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of culturing S.quadricauda strain SDEC-8, which involves (a) inoculating S.quadricauda strain SDEC-8 into bluegreen-11 medium (BG-11), and culturing the inoculum at 25 plus minus 1 degrees C, and light intensity of 2000-3000 Lux for 7 days, (b) transferring the resulting algal cells into second BG-11 medium, and expanding the culture cells at 25 plus minus 1 degrees C, light intensity of 2000-3000 Lux and aeration rate of 0.1-0.2 volume per volume per minute (vvm) for two days, (c) centrifuging the resulting culture cells, and (d) drying the supernatant to obtain algal powder.
NOVELTY - Preparing biogas comprises: (a) chopping 30-35 pts. switchgrass and 40-45 pts. sorghum straw, adding water to adjust concentration to 20%, acidifying at 30-40 degrees C for 5 days to obtain acidified feed solution; (b) adding 45-50 pts. livestock manure, 15-25 pts. biogas residue and 10-20 pts. biological bacteria into acidified feed solution, mixing and fermenting at 50-60 degrees C; and (c) collecting the thermostatic gas produced during fermentation.    USE - The method is useful for preparing biogas (claimed).    ADVANTAGE - The method has high biogas production rate.
NOVELTY - This utility new type claims a a light interference measuring instrument, comprising a measuring main body, a measuring device main body. measurement, the measuring main body inner has set with plane mirror group, prism group, reflection prism group and pneuma room group, a pneuma room group has a pneuma. inlet and outlet, wherein, the inlet and outlet pneuma device comprises air pump, said air pump comprises the first pipe and the second pneuma pneuma tube, said first tube a pneuma pneuma room group, said device main body is further set with has the first electromagnetic valve and the second electromagnetic valve, the first electromagnetic valve and silicon glue tube is filled with a silicon glue connected, the second electromagnetic valve and the medicine tube is a soda lime is filled soda lime connected, silicon glue medicine tube and the medicine tube connected soda lime. This device can conveniently and quickly for carrying out a gas, and without need to frequently is silicon glue for traditional Chinese medicine tube and soda lime medicine tube a splice, using is convenient and fast measurement of carbon dioxide and a concentration of.
NOVELTY - A doxorubicin lipid microbubble comprises gas carrier and doxorubicin-loaded albumin nanoparticles wrapped in phospholipid bilayer membrane in which albumin is bovine serum albumin.    USE - A doxorubicin lipid microbubble.    ADVANTAGE - Doxorubicin lipid microbubble is convenient to store and transport, removes free radicals, delays body aging, improves lipid metabolism and brain activity, enhances immune function, prevents and treats arteriosclerosis, promotes nerve conduction, promotes drug penetration, and has prolonged preservation time and drug effect time, reduced toxicity and side effects, and increased curative effect, and preparation is simple and environment-friendly and has high safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of doxorubicin lipid microbubble which involves preparing albumin aqueous solution and doxorubicin ethanol solution, slowly adding doxorubicin ethanol solution dropwise to albumin aqueous solution, adding glutaraldehyde, stirring, curing, performing rotary evaporation to remove ethanol and obtain drug-loaded albumin nanoparticle suspension, mixing phospholipid:glycerin:phosphate buffer solution with weight ratio of 55-60:5-8:100, adding drug-loaded albumin nanoparticle suspension, heating, filling with gas carrier, and oscillating.    DESCRIPTION OF DRAWING(S) - The drawing shows an optical microscope image of Doxorubicin lipid microbubble.
NOVELTY - A health care almond jujube soap comprises 200-300 pts. wt. palm oil, 50-100 pts. wt. pumpkin seed oil, 100-150 pts. wt. evening primrose oil, 150-300 pts. wt. purified water, 50-100 pts. wt. sodium hydroxide, 5-10 pts. wt. jasmine essential oil, 30-50 pts. wt. almond, 40-45 pts. wt. jujube, 10-15 pts. wt. stiff silkworm, 8-15 pts. wt. Radix bupleuri, 10-13 pts. wt. gordon euryale seed, 15-20 pts. wt. honeysuckle, 5-10 pts. wt. Houttuynia cordata, and 5-8 pts. wt. Lucid ganoderma.    USE - A health care almond jujube soap for removal of speckle and personal care product, beauty product, or cream product (all claimed).    ADVANTAGE - Process is environment-friendly, and product does not irritate skin, gently nourishes skin, and has beautifying and whitening effect, antibacterial effect, no allergic reaction and toxic side effect, and strong cleaning ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of health care almond jujube soap which involves mixing palm oil, pumpkin seed oil, and evening primrose oil into mixing dish, heating at 55 degrees C for 30 minutes under stirring condition to obtain mixed oil, stirring purified water and sodium hydroxide for 30 minutes, cooling at 55 degrees C to obtain alkali solution, pouring alkali solution into mixed oil, stirring for 60 minutes, adding jasmine essential oil, continuously stirring for 15 minutes, standing for 5 days to obtain soap, cleaning almond, jujube, stiff silkworm, R. bupleuri, gordon euryale seed, honeysuckle, H. cordata, and L. ganoderma, chopping, grinding to obtain traditional Chinese medicine powder having fineness of 100 meshes, heating obtained soap at 55 degrees C to dissolve, adding traditional Chinese medicine powder, stirring for 30 minutes, pouring into mold, drying with air, standing for 7 days, demolding, and packaging.
NOVELTY - This utility model relates to a marsh gas reaction tank and marsh gas happen circulation system. Wherein the marsh gas reaction tank, tank body comprises inner outside are coated with anti-corrosive layer, the tank body upper end is set with an inlet feed, wherein the feed port is provided with a human hole cover, on the human hole cover is set with pressure table, safety valve and gas transmission pipeline, a tank body side is provided with drain pipe, the drain pipe provided with wide upper and narrow lower expansion flow is as follows in a side part in the tank body, a drain pipe part provided with drain valve in tank body. application of a marsh gas reaction tank circulation happen in marsh gas reaction tank through a gas pipeline and water separator a pneuma, pneuma water separator through pipeline and marsh gas desulfurization purifier connected, marsh gas desulfurization water purifier through pipeline connected to a gas using device. The tank structure is simple, the installation is convenient and quick, a mobile, which is good for production.
NOVELTY - Antibacterial powder comprises natural quartz mineral raw materials carrier, which is loaded with silver nano-particles in a thickness of 20-50 nm, where the amount of silver particles loaded, is 0.05-0.3 g/g.    USE - Used as an antibacterial powder.    ADVANTAGE - The method utilizes easily available and low cost raw materials; is suitable for industrial production, and environmental friendly; and has simple operation procedure, high synthesis efficiency, and low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the powder, comprising (i) adding pure natural quartz mineral raw materials into a ball milling tank, carrying out ball-milling, and sieving, then drying the sieved slurry at 150 degrees C by placing in an oven, to obtain white powder; (ii) dispersing white powder in mixed solution of deionized water and ethanol, where the mass-volume concentration of white powder is 1:25, and magnetically stirring by adding 1-3 g/100 ml silver nitrate solution for 12 hours, and evaporating the mixture to dryness at 80-120 degrees C, to obtain dark green powder; and (iii) sintering dark green powder by placing in muffle furnace under atmospheric air, and naturally cooling to room temperature, to obtain the final product.
NOVELTY - The fuel cell module (1) has a fuel supply apparatus that is provided in the upstream of a vaporizer (7) to supply the raw fuel gas to the vaporizer. A modifier (9) is provided in the downstream of the vaporizer to modify the raw fuel gas to the fuel gas using the water vapor. A pressure regulation mechanism is provided to adjust the pressure between the fuel supply apparatus and the vaporizer.    USE - Fuel cell module equipped with fuel cells such as solid oxide fuel cell.    ADVANTAGE - Since the variation in a fuel-supply pressure can be suppressed, the fluctuation of the flow volume of the raw fuel gas supplied to a modifier is effectively suppressed. Since the flow volume of the fuel gas supplied to the fuel cell is fluctuated, the generated electric power is stabilized effectively. The failure of the apparatus by the dew condensation water generated by back flow of water vapor is effectively prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell module. (Drawing includes non-English language text)    Fuel cell module (1)    Heat insulation container (3)    Fuel-supply stack (5)    Vaporizer (7)    Modifier (9)
NOVELTY - The assembly (112) has a filter house comprising a filter element positioned within a portion and collecting solids entrained in liquefied natural gas (LNG) rich slurry (118) on a surface of the filter element. A valve is coupled to the portion. A cleaning system is coupled to the filter house, and removes the solids from the surface of the filter element. The valve is selectively actuated to facilitate removal of the solids from the surface of the filter element and to channel the solids from the portion through the valve.    USE - Filter assembly for use in a natural gas liquefaction system to convert natural gas e.g. methane, nitrogen and carbon dioxide (all claimed), into LNG used as fuel e.g. gasoline and diesel. Can also be used for converting hydrogen sulfide.    ADVANTAGE - The assembly purifies liquefied natural gas in an efficient manner and reduces cost by eliminating natural gas pretreatment systems that remove carbon dioxide before to natural gas liquefaction and an ecological footprint of the liquefaction system.    DETAILED DESCRIPTION - The filter element is fabricated from ceramic material and sintered metallic material. An INDEPENDENT CLAIM is also included for a method for operating a natural gas liquefaction system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a liquefaction system.    Natural gas liquefaction system (100)    Natural gas source (102)    Moisture removal system (104)    Filter assembly (112)    LNG rich slurry (118)
NOVELTY - The utility model relates to a moderate-high temperature full fermentation marsh gas device, said device provided with internal liquid storage tank, the liquid storage tank top end provided with guide hole, two side provided with a feeding window, the upper liquid storage tank set with material wherein, feeding wherein a feeding window connected, bottom liquid storage tank provided with a drain and a slag outlet, a bottom liquid storage tank provided with heating device, a liquid storage tank upper part with protecting the floating grid. The utility model is new type provide a set with a simple structure, low cost of liquid storage tank, using floating protecting grate, a liquid level higher than the protecting floating grate, the upper layer is not a layer structure, the stirring device, saves cost, is a dry substance content increase to 2-3 times, is a use does not need smashing straw, saves cost, thus under a same condition, a gas total quantity exponentially increase.
NOVELTY - This utility new type device relates to the field of medical device technology field, specifically is a new-type fat transplantation system A, a liposuction transplanting needle (1), a four-way valve (2), resin l (4), an injector (5), a silicon glue pipe (7), inserter (8) and the physiological saline bag (9), a four-way valve (2) is a seal interface, a four-way valve (2) of the other one interface connecting the resin l (4) in an injector (5), a four-way valve (2) is double of the other interface of inlet and outlet is, inlet and outlet of one-way according to need a seal a liposuction transplanting needle (1) and silicon glue pipe (7), silicon glue tube (7) of another end insert inserter (8) of one end, inserter (8) of another end insert physiological saline bag (9), the utility model is new type the same current technology, because of whole link thereof is d. to fat would not expose in air, reduces the fat is a pollute, ensures the survival rate of fat after fat transplant procedure.
NOVELTY - This utility new type claims a one disposable infusion device, the infusion set with air inlet device has a conduit front end of a puncture outfit, a puncture outfit, a jacket set connected in a puncture outfit, a conduit also has a set of three-way component with a dropping funnel, a flow regulator set connected in a conduit, the conduit end. Rubber injection element a vein infusion needle component, a vein infusion needle component has set with medicine liquid filter. A infusion tube between a puncture outfit and flow regulator, connected has a set of fixing a vein infusion needle component. The infusion apparatus a filter equipped with a vein infusion needle component on, can take all use vein injection medicine taking a to ensure the safety of vein injection medicine, at the same time, set connected fixedly a vein transfusion needle has a a a a a a infusion tube between puncture outfit and flow regulator, vein puncture component can is hung in a transfusion rack, it will not fall-pricking wound induced nurse and patient, but also ensures the vein puncture needle is not pollute.
NOVELTY - This utility new type relates to one used for a domestic sewage processing system of ship, comprising vacuum, vacuum, vacuum collection device and domestic sewage processing device, a vacuum collection device comprises box body, a pedestal, a double injection pump, a double injector and a double pipe, vacuum pipe comprises a horizontal pipe and vertical pipe, a horizontal pipe and vertical pipe connected, the level a vacuum toilet connecting pipe, a vertical pipe and vacuum collection device connected, the horizontal pipe and vertical pipe are set with a diaphragm valve, a discharge pipe and a domestic sewage processing device connected, the second discharge pipe extends out of ship, the domestic sewage treatment device provided with a double water outlet, after using a construction, this utility new type arrangement is flexible, it saves water source and peculiar smell.
NOVELTY - A biological teacher for a sample manufacture, comprising a desk body, a desk bottom set with holder, internal desk top set with table-board, wherein the said two side table-board set with lamp, a table top provided with a ring clamp, provided with two side of circular hole, circular hole is equipped with thin rubber glove, a desk use toughened glass is made, the top part is a open structure, the desk body set with water leakage hole at the bottom, a table provided with a level gauge, the utility new type has advantages of use is convenient, when teaching convenient for students to observe manufacture is sample, the hand would not pollute sample when manufacture, simple structure and practical effect.
NOVELTY - The gas detector (100) has a first gas sensor having a first gas specificity and a first response time, a second sensor having a second gas specificity and a second response time, and a readout and analysis circuit (118) coupled to the gas sensors, which reads and analyzes data from the gas sensors. A control circuit (120) coupled to the readout and analysis circuit and to the gas sensors, execute a logic that operates the first gas sensor, the second gas sensor, or both gas sensors.    USE - Gas detector used in e.g. indoor set-up, outdoor set-up for detecting presence and concentration of gas such as methane, carbon monoxide, carbon dioxide in air. Uses include but are not limited to mine, semiconductor facility, steel manufacturing facility, petrochemical facility.    ADVANTAGE - Produces faster, real-time detection result on total gas concentration for early warning on gas excursion. Enables real-time air monitoring since gas detection modes can be operated independently, simultaneously in parallel or in certain sequences based on sensing criteria. Utilized in semiconductor facility to ensure clean room air quality, ensuring the air is free of contaminants and improving process yield. Monitors the coke oven gas by-product leakage and process optimization in steel manufacturing facility. Identifies leaking gases and locates the source of leakage, which can provide immediate warning and emergency response actions, in a petrochemical facility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas analysis process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the gas detector.    Gas detector (100)    Substrate (102)    Pump (112)    Readout and analysis circuit (118)    Control circuit (120)
NOVELTY - The manufacturing method involves positioning sealing members (30) between an anode separator (13) and a cathode separator (14) or between the membrane electrode assemblies (11) which adjoin the adjacent separators. The sealing member seals the outer periphery of the membrane electrode assembly. The positioning members (40) are positioned inwardly than the sealing members between the separators or between the membrane electrode assemblies which adjoin the adjacent separators.    USE - Manufacturing method of fuel cell (claimed).    ADVANTAGE - Position of a separator with adjacent separator or membrane electrode assembly is rapidly fixed by positioning of the positioning members. Positioning member does not leak out outside by positioning inwardly than the sealing member. Precision and cycle time of lamination of the separators and membrane electrode assemblies are made compatible.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the manufacturing method of the fuel cell.    Membrane electrode assembly (11)    Anode separator (13)    Cathode separator (14)    Sealing members (30)    Positioning members (40)
NOVELTY - The apparatus (100) has an optical transmitting unit (110) for providing output light of a laser light source (150) to a measurement target. A control unit (170) analyzes reflection light (14). A frequency locking portion (112) fixes center frequency of the laser light source on a center of a specific absorption band. An optical receiving unit (140) receives the reflection light reflected by specific gas in the measurement target, and extracts a harmonic component of modulation frequency according to time. A beam extension part (115) increases beam size of the light.    USE - Apparatus for sensing leakage of gas such as methane, ethane, propane, helium or nitrous oxide gas, in a vacuum chamber, a container and a gas storage tank.    ADVANTAGE - The apparatus senses leakage gas for long distance using frequency modulation laser and stabilized differential signal and quickly detects a leaking position of the gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for sensing leakage of gas in a vacuum chamber, a container and a gas storage tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an apparatus for sensing leakage of gas in a vacuum chamber, a container and a gas storage tank.    Analyzes reflection light (14)    Gas leakage sensing apparatus (100)    Optical transmitting unit (110)    Frequency locking portion (112)    Beam extension part (115)    Optical receiving unit (140)    Laser light source (150)    Control unit (170)
NOVELTY - Extraction of docosahexaenoic acid and eicosapentaenoic acid comprises taking snailfish, freeze-drying, crushing into powder, grinding, sieving through 80 meshes sieve for 2 times, and drying; taking 50 kg snailfish meal, carrying out supercritical carbon dioxide fluid extraction with entrainer, where ratio of entrainer to snailfish meal in cosolvent is 1:1-1:4, installing reactor, and sealing; extracting at 18-30 MPa pressure and 38-54 degrees C temperature for 3 hours; and regulating pressure to 24-36 MPa, collecting extract at 40-60 degrees C, and separating.    USE - Method for extracting docosahexaenoic acid and eicosapentaenoic acid (claimed) used for medicine and health product.    ADVANTAGE - The docosahexaenoic acid content is 30-46 wt.% and eicosapentaenoic acid content is 24-40 wt.%. The method has high extraction rate, high safety, and low material cost and is stable, convenient, and environment-friendly.    DETAILED DESCRIPTION - Extraction of docosahexaenoic acid and eicosapentaenoic acid comprises taking snailfish, freeze-drying, crushing into powder, grinding, sieving through 80 meshes sieve for 2 times, and drying; taking 50 kg snailfish meal, carrying out supercritical carbon dioxide fluid extraction with entrainer, where ratio of entrainer to snailfish meal in cosolvent is 1:1-1:4, installing reactor, and sealing; extracting at 18-30 MPa pressure and 38-54 degrees C temperature for 3 hours; and regulating pressure to 24-36 MPa, collecting extract at 40-60 degrees C, and separating, where carbon dioxide flow rate is 2 mL/g and cosolvent is water, methanol, ethanol, acetone, or propane.
NOVELTY - Methane production system comprises a feeding tube (10), a discharging pipe (20), a fermentation pipeline (30), an air flowing pipe (31), air resistance plates (38). Methane producing bacteria pipeline (52) and methane producing fungus pipeline (53) are equipped in a methane production system. The methane producing bacteria and fungus strain along with fermentation raw material, are passed into a fermentation tank by the fermentation pipeline under a hydraulic pressure (40). Convection occurs, where the generated methane is stored in a methane gas accumulation area.    USE - Methane production system.    ADVANTAGE - The methane production system equipped with stirrer facilitates good slurry circulation performance. The methane production system equipped with deep fermentation system improves the methane gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane production system.    Feeding tube (10)    Discharging pipe (20)    Fermentation pipeline (30)    Air flowing pipe (31)    Air resistance plates (38)    Hydraulic pressure (40)    Methane producing bacteria pipeline (52)    Methane producing fungus pipeline (53)
NOVELTY - Methane fermentation system comprises a feeding pipe (10), a discharge pipe (20), a straighten base pipe (30), and a water pressure pipe (40). The circular shaped base pipe is stretched to form the straighten base pipe, where its both ends are mounted with the feeding pipe and the discharge pipe. The feeding pipe and the discharge pipe, are horizontally set with a drain pipe (42). Fermentation raw material is fed into the fermentation tank, and then processed under hydraulic pressure to generate methane using microbial strain.    USE - Methane fermentation system.    ADVANTAGE - The methane fermentation system promotes the fermentation of raw materials in the deep fermentation system, and thus improves the methane gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane fermentation system.    Feeding pipe (10)    Discharge pipe (20)    Straighten base pipe (30)    Water pressure pipe (40)    Drain pipe (42)
NOVELTY - Methane generation system comprises a feeding tube (10), a discharging pipe (20), a fermentation pipeline (30), air resistance plates (36,38). The methane generation system also comprises fermentation raw material feeding tube (42), a methane discharge tube (44), an exhaust pipe (46). The fermentation raw material feeding tube is horizontally set with methane discharge tube. Fermentation raw material and microbial strain, are inoculated into the fermenter to generate methane as biogas under hydraulic pressure.    USE - Methane generation system.    ADVANTAGE - The methane generation system promotes uniform distribution of microbial strain into the fermenter to yield larger volume of methane. Thus, the methane generation system increases the production rate of methane on large scale.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane generation system.    Feeding tube (10)    Discharging pipe (20)    Fermentation pipeline (30)    Air resistance plate (36,38)    Fermentation raw material feeding tube (42)    Methane discharge tube (44)    Exhaust pipe (46)
NOVELTY - Hair color composition comprises: (a) a flavonoid, which is (3S)-2-(3,4-dihydroxyphenyl)-3,5,7-trihydroxychroman-4-one compound with ethane (1:1) (I); (b) a catecholamine, which is substituted 2-(3,4-dihydroxyphenyl)-2-hydroxyethylamino compound (II); (c) a peroxidase enzyme; and (d) a hydrogen peroxide generator or hydrogen peroxide.    USE - The hair color composition is useful: in a kit for coloring hair (all claimed) to provide a darker color; and as a shampoo or hair conditioning composition, or a two-in-one conditioning shampoo composition.    ADVANTAGE - The hair color composition: when applied to natural white hair fibers, provides superior darkening than comparative compositions; and exhibits improved conditioning properties.    DETAILED DESCRIPTION - Hair color composition comprises: (a) a flavonoid, which is (3S)-2-(3,4-dihydroxyphenyl)-3,5,7-trihydroxychroman-4-one compound with ethane (1:1) of formula (I); (b) a catecholamine, which is substituted 2-(3,4-dihydroxyphenyl)-2-hydroxyethylamino compound of formula (II); (c) a peroxidase enzyme; and (d) a hydrogen peroxide generator or hydrogen peroxide.    R1, R2 = 1-5C, 1-3C, 1-2C optionally branched alkyl (optionally substituted with halide, -OH, -NH2 or O) or H.    INDEPENDENT CLAIMS are also included for:    (1) a kit for coloring hair comprising the hair color composition, and a pre- or post-treatment composition comprising a metal ion suitable for coordinating to (I) or the product of the reaction of technical features (a), (b), (c) and (d) as above per se; and    (2) coloring hair comprising the step of treating hair with the hair composition.
NOVELTY - Producing low sulfur propane and butane, comprises: reacting mercaptan in washed feed stream (18) with caustic stream (28) to produce mercaptan salt in rich caustic stream (30) and hydrocarbon treated stream (60); reacting mercaptan salt in rich caustic stream with oxygen and water to produce mixed caustic/disulfide stream (40); separating caustic and disulfides in mixed caustic/disulfide stream to produce disulfide stream and caustic stream; and fractionating the hydrocarbon treated stream to produce a propane stream, butane stream and more than 5 carbons containing stream.    USE - The method is useful for producing low sulfur propane and butane (claimed), more than 5 carbon containing product from 1 to more than 5 carbon containing feed stream.    ADVANTAGE - The method utilizes the apparatus and produces low sulfur propane and butane at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for apparatus for producing low sulfur propane and butane comprising: an extraction unit configured to react a mercaptan with caustic to form a mercaptan salt and produce a hydrocarbon treated stream and a rich caustic stream; a caustic regeneration unit fluidly coupled to the extraction unit, where the caustic regeneration unit is configured to react the mercaptan salt with oxygen and water to produce a disulfide; and a hydrocarbon fractionation zone fluidly coupled to the extraction unit, where the hydrocarbon fractionation zone is configured to fractionate hydrocarbons with 3 to more than 5 carbon atoms into a propane stream, a butane stream and more than 5 carbon containing stream.    DESCRIPTION OF DRAWING(S) - The figure illustrates schematic diagram of an apparatus and a method for producing a propane stream, a butane stream, and more than 5 carbons containing stream.    Washed feed stream (18)    Caustic stream (28)    Rich caustic stream (30)    Mixed caustic/disulfide stream (30)    Hydrocarbon treated stream (60)
NOVELTY - Process for converting waste fiber into solid fuel, involves providing a supply of animal waste including waste fiber in predetermined amount, subjecting the supply of animal waste to anaerobic digestion, producing a waste byproduct, dewatering the waste byproduct, and compressing the dewatered waste byproduct to form briquettes.    USE - Process for converting waste fiber into solid fuel (claimed) for producing energy.    ADVANTAGE - The waste byproduct produced by anaerobic digestion during conversion of waste fiber into solid fuel, efficiently produces sustainable and renewable energy, while reducing the depletion of natural resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating process for converting waste fiber into solid fuel.    Reception trough or pit (12)    Manure Slurry (14)    Inclined manure auger (20)    Sand separation device (22)    Storage area (30)
NOVELTY - Preparing (P1) aclidinium bromide (I), comprises: reacting (3R)-3 -hydroxy-1-(3-phenoxypropyl)-1-azoniabicyclo (2.2.2)octane bromide (III) with substituted hydroxy-di-thiophen-2-yl-acetic acid compounds (II) to form reaction mixture; and reacting the obtained reaction mixture with hydrogen bromide.    USE - The process is useful for preparing aclidinium bromide (claimed) which is used for treating bronchospasm associated with chronic obstructive pulmonary disease including bronchitis and emphysema. No biological data given.    ADVANTAGE - The process: provides aclidinium bromide that has a purity greater than 98% as determined by HPLC (claimed); and is simple, eco-friendly, cost-effective, reproducible, robust and well suited on commercial scale.    DETAILED DESCRIPTION - Preparing (P1) aclidinium bromide of formula (I), comprises: reacting (3R)-3 -hydroxy-1-(3-phenoxypropyl)-1-azoniabicyclo (2.2.2)octane bromide of formula (III) with substituted hydroxy-di-thiophen-2-yl-acetic acid compounds of formula (II) to form a reaction mixture; and reacting the obtained reaction mixture with hydrogen bromide.    R = aryl (optionally substituted), alkyl, cycloalkyl or alkylaryl, preferably methyl.    INDEPENDENT CLAIMS are also included for:    (1) purification of aclidinium bromide (I), comprising either (a1) providing a solution of aclidinium bromide in a solvent or its mixture or their aqueous mixtures, precipitating the solid from the solution and isolating the pure aclidinium bromide or providing a solution of aclidinium bromide in a polar aprotic solvent, adding an anti-solvent to the solution obtained to precipitate the solid aclidinium bromide and isolating the pure aclidinium bromide; and    (2) use of compound of formula (III) in the preparation of (I).
NOVELTY - The system has a reformer for reforming fuel. A heat exchanger is filled with the reformed fuel. A water supplying apparatus supplies moisture to the fuel. A fuel delivery unit supplies the fuel. An oxygen supply unit is provided with oxygen reactant to produce electricity. The heat exchanger is generated in a fuel cell stack module. A water level sensor is fixed on the water supplying apparatus to sense a water level within a water tank. A heater is provided with external energy to produce heat. A control unit controls operation of the heater according to state of moisture.    USE - Fuel cell system.    ADVANTAGE - The system utilizes the heat exchanger to supply the heat that is generated in the fuel cell stack module to the moisture without utilizing separate water-treatment apparatus. The system supplies the moisture from the water supplying apparatus to the reformer, so that energy reduction effect of the system can be achieved. The system improves reaction efficiency of unit battery cell due to temperature increment, so that occurrence if failure during electricity production can be prevented. The system has wide application range. The system removes impurity factors within moisture, so that overall stability of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system.'(Drawing includes non-English language text)'
NOVELTY - Biological matrix comprises 30-40 wheat straw 30-40, 25-35% corn straw, 8% pumice, 8-12% peat and 20-35% fermenting material. Biological matrix is prepared by crushing wheat straw, corn straw, pumice and peat and then adding water to obtain mixture. The fermenting material is added into mixture and then curing matrix is added to obtain another mixture. The obtained mixture is fermented to obtain fermentation material and then lime is added to adjust pH value of fermentation material, where water content of fermentation material is 30-40%.    USE - Biological matrix.    ADVANTAGE - The biological matrix is economic and stable, and does not pollute environment and, has high fertility.    DETAILED DESCRIPTION - Biological matrix comprises 30-40 wheat straw 30-40, 25-35% corn straw, 8% pumice, 8-12% peat and 20-35% fermenting material. Biological matrix is prepared by crushing wheat straw, corn straw, pumice and peat and then adding water to obtain mixture. The fermenting material is added into mixture and then curing matrix is added to obtain another mixture. The obtained mixture is fermented to obtain fermentation material and then lime is added to adjust pH value of fermentation material, where water content of fermentation material is 30-40%. Earthworm is added into fermentation material and then cured for two weeks. The fermentation material is filtered and then fermented to obtain another fermentation material. The obtained fermentation material is crushed and then dried to obtain dried material. Fertilizer is added into dried material to obtain the product.
NOVELTY - Preparing bio-organic fertilizer involves crushing 20-30 parts clover powder and 5-9 parts cotton seed hull through 200 meshes into powder. 5-9 parts Plant ash and 15-20 parts fly ash are mixed with powder and then 10-15 parts fish viscera is mixed and dried to reduce moisture to 40-50% to obtain a mixture. The mixture is diluted by utilizing 5% of phosphoric acid (1.5-2 times), and then 25-33 parts ammonium phosphate is added. The mixture is composting and then fermenting for 10-15 days by adding 0.5-1.2 parts fungus to obtain fermented product.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare mineral and nitrogen enriched bio-organic fertilizer that increases yield of crops.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer involves crushing 20-30 parts clover powder and 5-9 parts cotton seed hull through 200 meshes into powder. 5-9 parts Plant ash and 15-20 parts fly ash are mixed with powder and then 10-15 parts fish viscera is mixed and dried to reduce moisture to 40-50% to obtain a mixture. The mixture is diluted by utilizing 5% of phosphoric acid (1.5-2 times), and then 25-33 parts ammonium phosphate is added. The mixture is composting and then fermenting for 10-15 days by adding 0.5-1.2 parts fungus to obtain fermented product. The fermented product is dried crushed and then packaged to obtain final product.
NOVELTY - Method for preparing special fertilizer for flowers, involves (a) drying seaweed, immersing the seaweed in 95% ethanol, UV sterilizing immersed seaweed, and crushing the sterilized seaweed to obtain slurry, (b) uniformly mixing phosphorus, potassium and nitrogen fertilizer to obtain organic fertilizer, and (c) mixing the slurry obtained in step (a) with the organic fertilizer obtained in step (b), adding obtained mixture and biological bacteria to reaction kettle, regulating pH of obtained mixture, and uniformly stirring obtained product.    USE - The method is useful for preparing special fertilizer for flowers (claimed).    ADVANTAGE - The method improves immunity of flowers, and biological activity of soil, and resistance of flowers with respect to virus, bacteria, cold and drought, and enhances photosynthesis of plants.    DETAILED DESCRIPTION - Method for preparing special fertilizer for flowers, involves (a) drying seaweed, removing impurities from the seaweed, immersing the seaweed in 95% ethanol, UV sterilizing immersed seaweed, and crushing the sterilized seaweed to obtain slurry, (b) uniformly mixing phosphorus, potassium and nitrogen fertilizer to obtain organic fertilizer, where the fertilizer comprises 5-15% phosphorus, 5-15% nitrogen, 5-10% potassium, and the content of the phosphorus, potassium and nitrogen fertilizer is 25-35%, and (c) mixing the slurry obtained in step (a) with the organic fertilizer obtained in step (b), adding obtained mixture and biological bacteria to reaction kettle, regulating pH of obtained mixture, and uniformly stirring obtained product.
NOVELTY - Planting soil microorganism repairing agent comprises 1 pt. wt. composite microbial agent, 18-22 pts. wt. soil conditioning agent and 75-85 pts. wt. nutritional agent. The composite microbial agent comprises microorganism adsorbed on organic carrier. The microorganism comprises Trichoderma, Penicillium, Alcaligenes, Bacillus licheniformis and B. subtilis.    USE - Planting soil microorganism repairing agent used for repairing soil ecological system and degrading organic pollutants.    ADVANTAGE - The nutritional agent promotes the growth of microorganisms. The planting soil microorganism repairing agent shortens the soil repairing time, increases permeability of soil and quantity of oxygen in soil, is solid and easy to store and has long shelf life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of planting soil microorganism repairing agent comprising taking Pseudomonas, Trichoderma, Penicillium, Alcaligenes, B. licheniformis and B. subtilis, uniformly mixing to obtain composite microorganism, mixing with organic carrier to adsorb the microorganism on the organic carrier, obtaining composite microbial agent, and uniformly mixing with soil conditioning agent and nutritional agent to obtain the product.
NOVELTY - Organic substance-based composite fertilizer particle comprises 40-55% crop straw, 20-40% dry manure powder, 5-10% peat, 3-8% sapropel and 2-5% soybean cake fertilizer. The method comprises uniformly mixing the components, covering the mixture added into a mortar tank with a thin film, and stacking for 15 days under room temperature, fermenting, taking out, drying, placing the dried mixture into a pulverizer, and sieving through 60 meshes sieve, and humidifying the mixture, processing by placing the mixture for a granulating machine, to obtain large particles, and packaging, to obtain product.    USE - The fertilizer particle is useful for cultivating amaranth (claimed).    ADVANTAGE - The fertilizer particle is environmental friendly, rich in nutrients, and economical; has rapid effect, and long duration effect; and provides mineral nutrients required for growth of crops.
NOVELTY - Chicken manure, straw, watermelon vine, peanut meal and chitosan are mixed, fermented, monosodium glutamate wastewater containing sodium, phosphorus, potassium, glutamic acid, serine, leucine, tyrosine and amino acid, is added, mixed, and dried, to obtain mixture. Urea, slaked lime, potassium fulvate, nano non-metallic mineral material and sodium selenite, are added, and stirred. The resultant product is dried, pulverized, Trichoderma and effective microorganism bacteria are added, mixed, granulated, dried, sieved, and packed, to obtain composite fertilizer.    USE - Preparation of composite fertilizer used for treating and preventing pest insect and southern blight of tea tree.    ADVANTAGE - The composite fertilizer effectively suppresses pest.    DETAILED DESCRIPTION - Chicken manure, straw, watermelon vine, peanut meal and chitosan are mixed, fermented, monosodium glutamate wastewater containing 6-10% total of sodium, phosphorus and potassium, 2-4% glutamic acid, 0.2-0.5% serine, 0.4-0.6% leucine, 0.5-1% tyrosine and 4-8% amino acid, is added, mixed, and dried to moisture content of less than 60%, to obtain mixture. Urea, slaked lime, potassium fulvate, nano non-metallic mineral material and sodium selenite, are added to the resultant mixture, and stirred. The resultant product is dried, pulverized, Trichoderma and effective microorganism bacteria are added, mixed, granulated in a granulator, dried at low temperature, sieved, and packed, to obtain composite fertilizer.
NOVELTY - Bio-organic composite fertilizer comprises component A, component B and component C at 0.1-0.2:1:0.05-0.08 weight ratio.    USE - Bio-organic composite fertilizer used in agriculture (claimed).    ADVANTAGE - The bio-organic composite fertilizer has excellent water retention and long fertilization efficiency and enhances soil permeability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-organic composite fertilizer comprising mixing component A, component B and component C, adding into high-speed dispersion machine, uniformly dispersing, and obtaining the product.
NOVELTY - Organic nutrient liquid comprises 20 wt.% sword bean, 20 wt.% rice bran, 20 wt.% hyacinth, 10 wt.% bone powder, 10 wt.% sweet potato vine, 10 wt.% cucumber vine, 10 wt.% tomato leaves and 10 wt.% fermentation organism including Actinomycete, Aspergillus mauve, A.niger, Bacillus licheniformis, B.megaterium, red yeast, Lactobacillus and Azotobacter.    USE - The organic nutrient liquid is useful as fertilizer for planting vegetables.    ADVANTAGE - The liquid promotes the growth and yield of plant as it contains gibberellin, and increases weight of the finished product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for Organic nutrient liquid comprises 20 wt.% sword bean, 20 wt.% rice bran, 20 wt.% hyacinth, 10 wt.% bone powder, 10 wt.% sweet potato vine, 10 wt.% cucumber vine, 10 wt.% tomato leaves and 10 wt.% fermentation organism including Actinomycete, Aspergillus mauve, A.niger, Bacillus licheniformis, B.megaterium, red yeast, Lactobacillus and Azotobacter. The nutrient liquid is prepared by crushing the raw materials into fine powder, placing the mixture in a high temperature kettle, then adding rice bran and bone powder followed by fermentation bacteria, performing solid fermentation for 24 hours, then filtering the fermented material through 400 meshes sieve and sterilizing the liquid to obtain the product.
NOVELTY - A biological organic fertilizer comprises 30-35% total amount of nitrogen (N), phosphorus pentoxide (P2O5), and potassium oxide (K2O) at nutrient ratio N:P2O5:K2O of 6-15:5-18:6-25 and effective viable count of 0.5-1 billion/g, 15-25% organic matter, 0.15-0.2% nicotine, less than or equal to 3% chlorine ion, and less than or equal to 12% water in which fertilizer has fineness of 40-60 meshes and pH of 6-7.    USE - A biological organic fertilizer for preventing and treating lepidopteran pest and suppressing soil character transfer (all claimed).    ADVANTAGE - The fertilizer has high nitrogen phosphorus potassium inorganic nutrients and organic matter content, is environment-friendly, improves soil fertility, permeability, soil structure, and physical and chemical properties, enhances heat- and water-keeping ability, effectively suppresses occurrence of soil-borne pests and diseases, and has no peculiar smell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic fertilizer which involves grinding 40-60 pts. wt. tobacco, 10-20 pts. wt. vegetables, 20-30 pts. wt. pig manure, 5-10 pts. wt. humic acid, and 0.8-1.2 pts. wt. fermenting microorganism, stirring while adding water, uniformly mixing to obtain fermented material, uniformly mixing 50-60 pts. wt. fermented material, 21-23 pts. wt. urea, 15-17 pts. wt. monoammonium phosphate, 3-5 pts. wt. potassium chloride, 1-2 pts. wt. nano activated carbon powder, and 1-2 pts. wt. fermentation microbial inoculum, grinding into powder, sieving, and packaging.
NOVELTY - A bio-organic fertilizer comprises 8-15 pts. wt. biological fermentation broth, 50-80 pts. wt. organic material, 10-35 pts. wt. nitrogen-phosphorus-potassium fertilizer and 0.5-3 pts. wt. microfertilizer. The organic material comprises meal and/or chicken manure. The biological fermentation broth comprises 2-3 pts. wt. Azotobacter, 2-5 pts. wt. Rhizobium, 3-5 pts. wt. Bacillus, 1-2 pts. wt. phosphorus-solubilizing bacteria and 1.2-2 pts. wt. potassium-solubilizing bacteria.    USE - Bio-organic fertilizer is used for fertilizing tea leaves.    ADVANTAGE - The bio-organic fertilizer has excellent stability, seedling disease resistance and durability, and is rich in organic material and trace elements. The bio-organic fertilizer improves soil structure, solves problem of land compaction, effectively inhibits occurrence of pests, and increases production yield and quality of tea leaves.    DETAILED DESCRIPTION - A bio-organic fertilizer comprises 8-15 pts. wt. biological fermentation broth, 50-80 pts. wt. organic material, 10-35 pts. wt. nitrogen-phosphorus-potassium fertilizer and 0.5-3 pts. wt. microfertilizer. The organic material comprises meal and/or chicken manure. The biological fermentation broth comprises 2-3 pts. wt. Azotobacter, 2-5 pts. wt. Rhizobium, 3-5 pts. wt. Bacillus, 1-2 pts. wt. phosphorus-solubilizing bacteria and 1.2-2 pts. wt. potassium-solubilizing bacteria. The biological fermentation broth is obtained by separately culturing Azotobacter, Rhizobium, Bacillus, phosphorus-solubilizing bacteria and potassium-solubilizing bacteria and mixing.
NOVELTY - Preparing biological fertilizer involves drying and crushing dairy manure, chicken manure and pig manure to obtain mixture that is mixed with calcium oxide. The obtained mixture is fermented at 16-25 degrees C for 10-15 days to obtain fermented manure. Patrinia, colts foot, Morinda and rhizoma sparganii are dried, ground and sieved to obtain powder that is mixed with fermented manure to obtain mixed powder, which is fermented with strain at humidity of 55-60% for 10-15 days at 12-18 degrees C to obtain biological fertilizer.    USE - Method for preparing biological fertilizer (claimed).    ADVANTAGE - The method enables to prepare biological fertilizer that ensures good insecticidal effect and improved yield of crops.    DETAILED DESCRIPTION - Preparing biological fertilizer involves drying and crushing dairy manure, chicken manure and pig manure to obtain mixture that is mixed with calcium oxide. The obtained mixture is fermented at 16-25 degrees C for 10-15 days to obtain fermented manure. Patrinia, colts foot, Morinda and rhizoma sparganii are dried, ground and sieved to obtain powder that is mixed with fermented manure to obtain mixed powder, which is fermented with strain at humidity of 55-60% for 10-15 days at 12-18 degrees C to obtain biological fertilizer that comprises 50-65 pts. wt. dairy manure, 18-25 pts. wt. chicken manure, 35-42 pts. wt. pig manure, 5-8 pts. wt. calcium oxide, 1-3 pts. wt. Patrinia, 1.2-2 pts. wt. colts foot, 2-3.5 pts. wt. Morinda and 1-2.5 pts. wt. rhizoma sparganii.
NOVELTY - Production of garlic bio-organic fertilizer involves selecting water source, contracting fermentation tank, covering outer surface of the tank with polyurethane foam, mixing straw or broken sticks and dry leaves, with organic fertilizer, adding ordinary superphosphate, mixing, adding carbonized powder, binder, human waste, chicken manure, cow manure and pig waste, sealing, fermenting, adding organic material, calcium, magnesium, sulfur, zinc, copper, iron and trace elements, mixing, adding fly ash and fish bone, dehydrating, desulfurizing, crushing, screening, and packing.    USE - Production of garlic bio-organic fertilizer (claimed).    ADVANTAGE - The garlic bio-organic fertilizer is produced with improved soil organic matter content, soil physical property and fertilizer efficiency.    DETAILED DESCRIPTION - Production of garlic bio-organic fertilizer involves selecting water source, contracting fermentation tank with length of 40 m, width of 3 m and depth of 1.2 m, covering outer surface of the tank with polyurethane foam, mixing straw or broken sticks and dry leaves, with organic fertilizer, adding ordinary superphosphate, mixing, adding carbonized powder and binder, adding water to make the straw wet, adding human waste, chicken manure, cow manure and pig waste to increase nitrogen content, sealing with plastic film for 5-8 days, accumulating for 20 days, fermenting, ventilating, adding organic material, calcium, magnesium, sulfur, zinc, manganese, copper, iron and trace elements, mixing, adding 20-30 kg diammonium phosphate and 20-30 kg potassium sulfate, mixing, adding fly ash to increase potassium content and fish bone to increase calcium content, drying, dehydrating, desulfurizing, crushing, screening, and packing. The organic material is humic acid.
NOVELTY - Extraction of American cockroach nymphs molt comprises collecting American cockroach nymphs molt, naturally drying, crushing, sieving and soaking in ethanol to prepare powder mixed liquid; extracting under reflux, adding 5 times ethanol, extracting for 5 hours, adding 4 times ethanol, extracting for 4 hours, filtering, taking filtrate and concentrating; adding 8 times purified water, stirring at stirring speed of 40 revolutions/minute (rpm) and standing to obtain oil-water layer; and filtering lower water layer by filter paper and concentrating filtrate to obtain extract.    USE - Method for extracting American cockroach nymphs molt (claimed).    ADVANTAGE - The method avoids waste of American cockroach, increases utilization rate of resource and reduces environmental pollution. It has simple process, low device investment and high economical benefit.    DETAILED DESCRIPTION - Extraction of American cockroach nymphs molt comprises:    (A) collecting American cockroach nymphs molt, naturally drying, crushing, sieving by 24-mesh sieve screen to obtain powder and soaking in 90-95% ethanol to prepare powder mixed liquid;    (B) extracting under reflux at 75-80 degrees C, adding 5 times of 90-95% ethanol, extracting for 5 hours, adding 4 times of 90-95% ethanol, extracting for 4 hours, filtering, taking filtrate and concentrating at - 0.05 to - 0.06 MPa and 50-60 degrees C to obtain concentrated liquid with specific gravity of 1.05-1.15;    (C) adding 8 times purified water, stirring at 85-95 degrees C for 40 minutes at stirring speed of 40 rpm and standing for 4 hours to obtain oil-water layer; and    (D) filtering lower water layer by filter paper and concentrating filtrate at - 0.05 to - 0.06 MPa and 60-80 degrees C to obtain extract with specific gravity of 1.25-1.35.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of extraction of American cockroach nymphs molt (Drawing includes non-English language text).
NOVELTY - Producing agrocombustible solid from organic compounds, comprises: producing energy in the form of heat by transformation of organic materials; and producing agrocombustible solid, where the heat generated during the energy production step is partially utilized during the production step of agrocombustible solid by drying and granulating the organic compounds.    USE - The method is useful for producing agrocombustible solid.    ADVANTAGE - The method allows for recovery and reuse of heat, and provides the agrocombustible solid by utilizing the plant and/or animal derived organic materials, preferably biomass and animal waste, hence it is energy efficient and economical.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS aer also included for:    (1) a system for producing the agrocombustible solid from organic compounds, comprising at least one unit for producing energy as heat by transformation of organic materials, and at least one unit for producing agrocombustible solid, where the heat produced by the energy production unit is partially used up by the agrocombustible solid production unit for drying and granulating of organic compounds; and    (2) agrocombustible solid comprising organic material and the digestate obtained by transformation of the organic material and/or compost, where it is dried, ground and pressed into granules.
NOVELTY - Preparation of propargite comprises mixing organic solvent and propargite wet product, performing distillation and dehydration; injecting with carrier solvent, heating or film evaporating, distilling, dehydrating, wet grinding, modulating, packaging; complexing mancozeb and zinc in organic solvent, dehydrating and forming crystals.    USE - Method for preparing propargite (claimed).    ADVANTAGE - The method reduces decomposition, harmful impurities and dust pollution and avoids generating fire accident.
NOVELTY - A mancozeb is prepared by taking organic solvent and mancozeb, mixing, adding zinc, dehydrating, distilling, heating, evaporating, crushing, modulating, and packing.    USE - Method for preparing mancozeb (claimed).    ADVANTAGE - The product is environment-friendly.
NOVELTY - A wet product mix is distillation-dehydrated using an organic solvent. The resulting mixture with carrier solvent is heated or heating-distillation-dehydrated in film evaporator, dehydrated, wet-ground, modulated and packaged for continuous operation. A solution containing mancozeb, zinc complexes and an organic solvent is added to mixture and dehydration-crystal transformed, to obtain carboxin.    USE - Preparation of carboxin (claimed).    ADVANTAGE - The method enables preparation of carboxin, with reduced decomposition of product, harmful impurities and dust pollution, and without fire accidents.
NOVELTY - Preparation of binapacryl crystal involves taking binapacryl in organic solvent, performing distillation, evaporating, crushing, performing mancozeb and zinc complexation reaction in organic solvent and crystallizing.    USE - Method for preparing binapacryl crystal used as fungicide.    ADVANTAGE - The method reduces harmful impurity and dust, reduces decomposition reaction, and minimizes occurrence of fire accidents.
NOVELTY - Preparation of pyridaben comprises mixing organic solvent and pyridaben wet product, distilling to carry out dehydration, spraying into film evaporator, heating or distilling to carry out dehydration, wet grinding, modulating, and packaging; and adding mancozeb and zinc dissolved in organic solvent, and performing crystal dehydration process.    USE - Method for preparation of pyridaben (claimed).    ADVANTAGE - The method reduces decomposition of harmful impurity and dust pollution, and avoids fire accident generation in product drying process.
NOVELTY - Preparing malathion comprises (i) mixing organic solvent and malathion wet product, distilling and dehydrating, (ii) taking solvent as carrier, spray heating or film evaporator heating distillation dehydration, carrying out dehydration process and wet smashing, modulating, package process continuous operation, and (iii) complexing mancozeb and zinc, dehydrating and carrying out crystal transformation process in organic solvent.    USE - The method is useful for preparing malathion (claimed).    ADVANTAGE - The method reduces harmful impurities and dust pollution, and avoids the occurrence of product drying process fire accident.
NOVELTY - Organic-inorganic compound fertilizer comprises 10-20 pts. wt. bamboo shoot shell, 30-40 pts. wt. chicken manure, 10-20 pts. wt. nitrogenous fertilizer, 5-10 pts. wt. phosphate fertilizer, 6-12 pts. wt. potassium fertilizer, 1-10 pts. wt. clay containing high calcium, silicon oxide and trace element.    USE - Organic-inorganic compound fertilizer used for planting tree.    ADVANTAGE - The organic-inorganic compound fertilizer improves soil structure, increases permeability fertility, nutrient utilization, and biological activity, and reduces fertilizer loss from surface of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic-inorganic compound fertilizer, which involves:    (A) drying bamboo shoot shell to reduce water content to 10% and then crushing to obtain powder with particle size of less than or equal to 2mm;    (B) fermenting the bamboo shoot shell powder and and chicken manure with water content 30% by adding yeast through heat preservation for 25 days; and    (C) drying the fermented material and then mixing remaining components.
NOVELTY - An aerobic microorganism composite bacteria-containing biological product comprises aerobic microorganism composite bacteria loaded on porous carrier in which aerobic microorganism composite bacteria comprises Bacillus and Pseudomonas putida.    USE - An aerobic microorganism composite bacteria-containing biological product for sewage treatment (claimed).    ADVANTAGE - Aerobic microorganism composite bacteria-containing biological product improves biological treatment efficiency and water quality and reduces residual sludge production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of aerobic microorganism composite bacteria-containing biological product which involves soaking porous carrier in acid or alkali, rinsing with water until neutral to obtain pretreated porous carrier, and loading with aerobic microorganism composite bacteria; and    (2) sewage treatment which involves placing 10-50 vol.% aerobic microorganism composite bacteria-containing biological product in fixed bed or fluidized bed and performing sewage treatment in aerobic reaction tank in which sewage is municipal sewage and cultivation sewage.
NOVELTY - Preparing organic fertilizer involves taking chicken excrement and then sterilizing using ozone. 6-16 pts. wt. Solid nitrogen bacteria are added into 1000 pts. wt. chicken excrement and then stirred to obtain mixture, where humidity of mixture is 40-96%. The mixture is fermented at 1-40 degrees C for 10-46 days in anaerobic condition to obtain the product.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to convert chicken excrement into valuable organic fertilizer that prevents environment pollution, protects ecological environment, and promotes healthy development of farming industry, and has good economic value and wide market prospect.
NOVELTY - Microbial fertilizer comprises 100-120 pts. wt. chicken manure, 10-13 pts. wt. rice, 1-2 pts. wt. cuttlebone, 2-6 pts. wt. sea pumice, 5-9 pts. wt. cortex mori radicis, 4-10 pts. wt. Ginkgo, 2-6 pts. wt. maidenhair tree, 3-6 pts. wt. wheat flour, 5-9 pts. wt. fish meal, 16-25 pts. wt. peptone, 3-9 pts. wt. grass powder, 5-9 pts. wt. sodium aluminum phosphate, 2-6 pts. wt. calcium phosphate, 19-21 pts. wt. calcium pyrophosphate, 5-9 pts. wt. humic acid and 0.01-0.03 pts. wt. Verticillium powder.    USE - Microbial fertilizer.    ADVANTAGE - The microbial fertilizer provides multiple nutrients to plant because of micro-organism.
NOVELTY - Fertilizer comprises 50-60 pts. wt. peat, 15-23 pts. wt. cornmeal, 11-16 pts. wt. rose wood, 0.01-0.02 pts. wt. marine gryphiswaldense powder, 0.01-0.02 pts. wt. Beauveria bassiana powder, 0.1-0.2 pts. wt. Metarrhizium anisopliae powder, 50-80 pts. wt. manure, 0.01-0.02 pts. wt. trace element, 5-9 pts. wt. sodium dihydrogen phosphate, 2-7 pts. wt. disodium hydrogen phosphate, 3-8 pts. wt. sodium phosphate and 16-20 pts. wt. ammonium citrate.    USE - Fertilizer.    ADVANTAGE - The fertilizer improves soil quality and soil fertility, and has high efficiency and causes no pollution.
NOVELTY - Microbial fertilizer comprises 0.01-0.02 pts. wt. bacteria powder, 0.01-0.02 pts. wt. Bacillus cereus powder, 30-45 pts. wt. potato straw stick, 50-60 pts. wt. duck manure, 11-16 pts. wt. diammonium phosphate, 35-40 pts. wt. peat, 1-2 pts. wt. humic acid, 0.2-0.3 pts. wt. honeysuckle, 0.6-1.3 pts. wt. tuckahoe, 0.01-0.04 pts. wt. nitrifying bacteria powder and 0.01-0.02 pts. wt. Rhizobium powder.    USE - Microbial fertilizer used for increasing soil organic matter (claimed).    ADVANTAGE - The microbial fertilizer is prepared in a simple, eco-friendly and cost-effective manner, and long-acting effect, improves quality and structure of the soil, restrains soil-borne disease, and has wide industrial applicability.
NOVELTY - Deep purification of alkane comprises reacting alkane with alkaline solution, contacting with copper-containing adsorbent, and contacting with adsorbent for selective adsorption of polar compounds.    USE - Method for deep purification of alkane (claimed), particularly fluid catalytic cracking (FCC) 3-5C alkane fraction.    ADVANTAGE - The method makes FCC 3-5C alkane fraction suitable for conversion to propylene, isobutene, or pentene; increases olefin production yield; increases service life of alkane dehydrogenation catalyst and reduces consumption; and improves economic efficiency and downstream dehydrogenation process operation.
NOVELTY - Preparation of hydroxy dimetridazole involves mixing 1-methyl-5-nitroimidazole and an aqueous solution of formaldehyde or paraformaldehyde in a reaction vessel, stirring the mixture, heating the mixture at 130-140 degrees C and a pressure of 0.2-0.3 MPa for 5-15 hours, filtering the obtained product and then concentrating under reduced pressure.    USE - The method is useful for preparing hydroxy dimetridazole (claimed).    ADVANTAGE - The method is capable of easily preparing a block-shaped and yellow hydroxy dimetridazole with reduced usage of toxic solvents in a safe, economical, and environmentally-friendly manner.
NOVELTY - Chain-shaped alkane is prepared by adding raw material lignin, metal catalyst, and non-polar solvent to autoclave and reacting at 60-500 degrees C under hydrogen pressure of 0.1-10 MPa for 0.1-48 hours in which metal catalyst comprises hydrogenation deoxidation metal active center (M1) and ring-opening metal active center (M2), and alkane is 4-9 carbon-containing straight-chain and/or branched alkane.    USE - Preparation of chain-shaped alkane (claimed).    ADVANTAGE - Preparation of chain-shaped alkane is simple, low-cost, and efficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of chain-shaped alkane which involves adding 1st metal catalyst, lignin, and non-polar solvent to autoclave, reacting at 60-500 degrees C under hydrogen pressure of 0.1-10 MPa for 0.1-48 hours to form cycloalkane, separating to obtain cycloalkane, adding with 2nd metal catalyst and non-polar solvent to autoclave, and reacting at 60-500 degrees C under hydrogen pressure of 0.1-10 MPa for 0.1-48 hours in which 1st metal catalyst is M1 and 2nd metal catalyst is M2; and    (2) metal catalyst comprising M1 and M2.
NOVELTY - Method for preparing organic fertilizer involves (a) mixing lactic acid bacteria, bifidobacteria, actinomycetes and water, adjusting pH, and fermenting mixture, (c) heating mixture e.g. glutaraldehyde, diatomite, mixing the resulting product with fermentation broth, (d) crushing the resulting product, and mixing the crushed particles with organic manure, and (d) adding lime and water to the obtained mixture and stacking the mixture to obtain product.    USE - The method is useful for preparing organic fertilizer (claimed).    DETAILED DESCRIPTION - Method for preparing organic fertilizer involves (a) mixing lactic acid bacteria, bifidobacteria, actinomycetes and water in mass ratio of 1:1:1:3, adjusting pH of the resulting mixture to 3-5, and fermenting the resulting mixture at 60-70 degrees C for 2-3 hours, (c) heating mixture comprising glutaraldehyde, diatomite and nitrogen benzidine at 35-40 degrees C for 24-48 hours, mixing the resulting product with fermentation broth obtained in the step (a) and heating the mixture at 55-60 degrees C for 1-2 hours, (d) crushing the resulting product to have particle size of 5-10 mm, and mixing the crushed particles with organic manure, and (d) adding lime and water to the obtained mixture and stacking the mixture to obtain product.
NOVELTY - Organic fertilizer is prepared using 40-60 wt.% wastewater residue, 30-35 wt.% bulking agent, 5-10 wt.% gypsum, 2-7 wt.% calcium nitrate, 2-7 wt.% diammonium phosphate, and 1 wt.% microbial inoculum.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is simple and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the organic fertilizer, which involves weighing above-mentioned raw materials, drying the weighed raw materials to have moisture content of 5% or less, crushing the dried raw materials to have 0.1 mm sized particles, and fermenting the resulting mixture to obtain product.
NOVELTY - This utility new type provide a one kitchen garbage conversion device. The kitchen garbage conversion device comprising a box body, a box body is set with side feed wherein has. Inner box body has set with spraying device, and set with a microorganism in a liquid storage box is a box body connected. Tank body is a upper end surface has set with soil inlet, the other upper side is set with discharging wherein has. A feeding port, a discharging wherein, soil feeding port are set with the matching and a cover and seal ring. This utility new type has simple structure, a convenient use, conveniently a process family in daily life of kitchen garbage, the conversion is culture soil, effective use of the effective component of kitchen garbage, a the use of a resource.
NOVELTY - Usage method of phosphogypsum involves adding ammonia to sodium silicate solution, adjusting pH of resultant mixture, adding sodium phosphate, adding phosphogypsum, stirring, dissociating rare-earth ions in resultant mixture, leaching, performing solid-liquid separation, adding oxalic acid, adjusting pH of resultant mixture, filtering, adding ammonium bicarbonate to filtrate, adjusting pH of resultant mixture, separating supernatant, desalting precipitate, separating residue (A) and rare-earth carbonate concentrate, and drying rare-earth carbonate concentrate.    USE - Usage method of phosphogypsum for preparing calcium phosphate mineral organic fertilizer (claimed).    ADVANTAGE - The calcium phosphate mineral organic fertilizer is manufactured by economical and environmentally-friendly process, with high yield, using phosphogypsum.    DETAILED DESCRIPTION - Usage method of phosphogypsum involves adding ammonia to sodium silicate solution, adjusting pH of resultant mixture to 8-10 using sodium hydroxide solution, adding sodium phosphate, adding phosphogypsum, stirring, dissociating rare-earth ions in resultant mixture, adjusting pH of resultant mixture to 3.5-5.5, leaching, performing solid-liquid separation, adding oxalic acid, adjusting pH of resultant mixture to 2-3.5, filtering, adding ammonium bicarbonate to filtrate, adjusting pH of resultant mixture to 7-7.5, leaving still, separating supernatant, desalting precipitate separating residue (A) and rare-earth carbonate concentrate, and drying rare-earth carbonate concentrate.
NOVELTY - Fertilizer is prepared using 110-130 parts mass chicken manure, 50-60 parts mass weathered coal, 40-50 parts mass peat, 30-40 parts mass phosphate, 20-30 parts mass potassium mineral powder, 40-50 parts mass wheat flour, 15-17 parts mass water bug, 15-17 parts mass banana peel, 20-30 parts mass chicken waste, 20-30 parts mass donkey bone meal, 22-24 parts mass bamboo shoot peel, and 170-190 parts mass water.    USE - As fertilizer for purple leaf peach.    ADVANTAGE - The fertilizer is nontoxic and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves (a) weighing above-mentioned raw materials and crushing the weighed raw materials except water, (b) mixing the obtained powder with water, (c) fermenting the resulting mixture for 2-4 days, (d) allowing the resulting fermentation product to stand for 13 hours, and (e) granulating the mixture to obtain product.
NOVELTY - A coated fertilizer contains 7-12 pts. wt. molasses, 8-12 pts. wt. urea, 10-13 pts. wt. rock phosphate, 33-36 pts. wt. wheat bran, 2-3 pts. wt. borax, 7-13 pts. wt. ethyl cellulose, and 4-6 pts. wt. soil improving agent. The soil improving agent contains 10-15 pts. wt. zinc sulfate, 10-15 pts. wt. medical stone, 0.2-0.3 pt. wt. nanocarbon powder, 1-2 pts. wt. KH-550 (RTM: ( gamma )-aminopropyltriethoxysilane), 10-12 pts. wt. ferrous sulfate, 3-6 pts. wt. chlorinated paraffin, 0.3-0.6 pt. wt. selenium yeast and 1-2 pts. wt. oyster shell nanopowder.    USE - Coated fertilizer is used for strawberry flowering.    ADVANTAGE - The coated fertilizer prompts more strawberry flowering, maintains nutrition balance, and increases nutrient absorbability and disease resistance.    DETAILED DESCRIPTION - Coated fertilizer contains 7-12 pts. wt. molasses, 1-2 pts. wt. ammonium molybdate, 5-7 pts. wt. amino acid powder, 1-2 pts. wt. sodium polyacrylate, 10-13 pts. wt. slag, 1-2 pts. wt. gelatin, 1-3 pts. wt. castor oil, and water. The soil improving agent contains 10-15 pts. wt. zinc sulfate, 10-15 pts. wt. medical stone, 1-2 pts. wt. KH-550 (RTM: ( gamma )-aminopropyltriethoxysilane), 10-12 pts. wt. ferrous sulfate, 3-6 pts. wt. chlorinated paraffin, 0.3-0.6 pt. wt. selenium yeast, 1-2 pts. wt. oyster shell nanopowder, 1-2 pts. wt. borax, and 2-3 pts. wt. chitosan sugar. The components (except chlorinated paraffin) for soil improving agent are ground, and stirred for 30 minutes before granulation. The granulated particles are added to a roll package clothing pot and maintained at 45-50 degrees C. Molten chlorinated paraffin is sprayed on the surface of the particles to form a uniform coating, and dried at room temperature to obtain the soil improving agent. An INDEPENDENT CLAIM is included for preparation of coated fertilizer.
NOVELTY - Fertilizer is prepared using 15-17 parts mass nitrogen, 8-10 parts mass phosphate, 10-12 parts mass potash, 40-60 parts mass chicken manure, 20-24 parts mass humic acid, 20-30 parts mass pomegranate rind, 10-14 parts mass oil residue, 8-10 parts mass herba houttuyniae, 40-50 parts mass plant ash, 30-40 parts mass shell powder, 3-5 parts mass fermented organic manure, and 60-80 parts mass water.    USE - As fertilizer for wheat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves (a) weighing above-mentioned raw materials and crushing the weighed raw materials except water, (b) mixing the obtained powder with water, (c) fermenting the resulting mixture for 2-4 days, (d) allowing the resulting fermentation product to stand for 15 hours, and (e) granulating the mixture to obtain product.
NOVELTY - A honokiol is prepared by crushing Magnolia officinalis cortex, adding purified water in which weight ratio of M. officinalis cortex and purified water is 1:8-10, processing using high-speed cutting emulsifying machine at speed of 8000-12000 rpm for 10-20 minutes, processing 2-4 times using high-pressure micro-jet ultrafine grinding device at 25 degrees C and pressure of 80-120 MPa to obtain pasty liquid, adding diluted alkali solution, oscillating at 40-50 degrees C and power of 150-200 W for 20-30 minutes, washing with purified water until pH is neutral, and filtering.    USE - Preparation of honokiol (claimed).    ADVANTAGE - Process is simple, low cost, and environment-friendly, and has high product quantity, and high extraction rate.    DETAILED DESCRIPTION - A honokiol is prepared by crushing M. officinalis cortex, adding purified water in which weight ratio of M. officinalis cortex and purified water is 1:8-10, processing using high-speed cutting emulsifying machine at speed of 8000-12000 rpm for 10-20 minutes, processing 2-4 times using high-pressure micro-jet ultrafine grinding device at 25 degrees C and pressure of 80-120 MPa to obtain pasty liquid, adding diluted alkali solution, oscillating at 40-50 degrees C and power of 150-200 W for 20-30 minutes, washing with purified water until pH is neutral, filtering to obtain M. officinalis extract, adding petroleum ether in which weight ratio of extract and petroleum ether is 1:3-4, boiling, maintaining heat for 10 minutes, hot-filtering, drying filtrate using anhydrous sodium sulfate (Na2SO4), concentrating petroleum ether solution, cooling, crystallizing to obtain crude product, recrystallizing, and drying.
NOVELTY - Automotive grade urea is prepared by reacting carbon dioxide and ammonia with molar ratio of 1:3.6-5 in pressurized urea synthesis tower at 150-200 degrees C to obtain reaction solution, steam stripping excess ammonia and unconverted carbamate, decomposing, vacuum concentrating reaction solution to greater than or equal to 99.75 mass% molten urea with less than or equal to 0.25 mass% biuret with respect to molten urea, processing industrial water to high resistivity of 19-20 M Omega , mixing molten urea with high resistivity water to obtain 31.8-33.2 wt.% crude automotive grade urea, and ultrafiltering.    USE - Preparation of automotive grade urea for removing nitrogen oxide.    ADVANTAGE - Process is efficient, low cost, environment-friendly, and yields value-added automotive-grade urea.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of preparation of automotive grade urea. (Drawing includes non-English language text).
NOVELTY - A polymerized rosin diglycidyl ester epoxy resin comprises symmetric rosin derivative.    USE - Polymerized rosin diglycidyl ester epoxy resin (claimed).    ADVANTAGE - Resin has excellent UV resistance. Preparation is simple, environment-friendly, easy to operate, and uses raw materials from renewable resources.    DETAILED DESCRIPTION - A polymerized rosin diglycidyl ester epoxy resin comprises symmetric rosin derivative of formula (I).    R=aliphatic carbon chain optionally having ether bond.    An INDEPENDENT CLAIM is included for preparation of polymerized rosin diglycidyl ester epoxy resin which involves melting polymerized resin under inert gas atmosphere, adding molten diglycidyl ether, esterifying at 150-250 degrees C for 4-8 hours in presence of catalyst until acid value decreases to less than or equal to 5 mgKOH/g, and cooling.
NOVELTY - Extracting ellagic acid involves pulverizing or crushing pomegranate rind, adding pure water to pomegranate rind material, processing mixture in high speed emulsifying machine at 8000-12000 revolutions per minute for 10-20 minutes, and then processing the mixture in super-micro pulverizing device at 25 degrees C and 80-120 megapascal for two times to obtain extract. The extract is kept in a high pressure tank, and the purified water is added into the high pressure tank. The mixture is processed for 10-15 minutes, and then hydrolyzed to obtain concentrate.    USE - Method for extracting ellagic acid from pomegranate rind (claimed).    ADVANTAGE - The method enables to extract ellagic acid from pomegranate rind in a simple and eco-friendly manner.    DETAILED DESCRIPTION - Extracting ellagic acid involves pulverizing or crushing pomegranate rind, adding pure water to pomegranate rind material, processing mixture in high speed emulsifying machine at 8000-12000 revolutions per minute for 10-20 minutes, and then processing the mixture in super-micro pulverizing device at 25 degrees C and 80-120 megapascal for two times to obtain extract. The extract is kept in a high pressure tank, and the purified water is added into the high pressure tank. The mixture is processed for 10-15 minutes, and then hydrolyzed to obtain concentrate. Concentrated sulfuric acid is added to concentrate, and then precipitated with triethylamine. The pH value of solution is adjusted to 1-5. The solution is crystallized, filtered and dried to obtain light yellow powder.
NOVELTY - The group comprises raw material that is selected from 5-15 pts. wt. first polymer matrix, 5-10 pts. wt. second polymer matrix, 10-50 pts. wt. third polymeric matrix, 3-5 pts. wt. toughening agent, 1-5 pts. wt. first adsorbent, 25-50 pts. wt. second adsorbent, 300-600 pts. wt. water and 30-50 pts. wt. biological active component, where the first polymer matrix is selected from acid-resistant plant polysaccharide solution, the second polymer matrix is selected from alkali solution plant polysaccharide and the third polymeric matrix is selected from gelatin.    USE - Artificial glue group for high concentration organic waste water treatment process and natural water in-situ repair and sludge treatment process.    ADVANTAGE - The group has stable property, high degradation efficiency and high sludge yield, and avoids organic pollution.    DETAILED DESCRIPTION - The toughening agent is selected from starch i.e. branched starch, the first adsorbent is selected from active carbon powder and the second adsorbent is selected from sodium base bentonite. The acid-resistant plant polysaccharide solution is selected from agar, sodium alginate and pectin. The alkali solution plant polysaccharide is selected from sodium carboxymethyl cellulose, mannan and glue. An INDEPENDENT CLAIM is also included for an artificial glue group preparation method.
NOVELTY - An acetylene hydrogenation ligand-modified palladium supported catalyst comprises 1-3 wt.% palladium active component, organic-modified silica powder containing nitrogen and sulfur radicals, alkyl thiol ligand, and tetrabutylammonium borohydride reducing agent. A palladium salt is used comprising 0.01 g palladium chloride or palladium nitrate dissolved in 5-10 mL toluene solvent. The molar ratio of ligand and palladium is 1:1-3:1.    USE - Acetylene hydrogenation ligand-modified palladium supported catalyst.    ADVANTAGE - The catalyst can effective regulate and control its catalytic performance, and it has acetylene conversion rate of 100%, selectivity of 90% and stable performance under a relatively lower and higher reaction temperatures than hydrogen alkyne conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of ligand-modified supported palladium catalyst comprises dissolving palladium salt in toluene, adding alkyl thiol ligands, clarifying through ultrasonic vibration, adding tetrabutylammonium borohydride and organic-modified silica powder, constantly stirring until solvent evaporates, filtering, washing, and vacuum-drying.
NOVELTY - Methane is produced by uniformly mixing 30-35 pts. wt. pig manure and 40-45 pts. wt. dairy manure, low temperature acidifying at 35-38 degrees C to obtain mixed acidified material liquid, adding water to adjust acidified material liquid concentration to 15%, uniformly mixing with 15-20 pts. wt. crop straw, 15-25 pts. wt. mushroom, and 10-20 pts. wt. biological bacteria, constant temperature fermenting at 28-30 degrees C, and collecting constant temperature fermentation gas.    USE - Production of methane (claimed).    ADVANTAGE - The process is prolonged, effective, and continuous, and has increased production rate.
NOVELTY - A fuel cell system (100) comprises hydrogen generator (1) which produces hydrogen-containing gas, fuel cell (2), 1st oxygen-containing gas supply path (3) into which oxygen-containing gas supplied to hydrogen generator flows, 2nd oxygen-containing gas supply path (4) into which oxygen-containing gas flows and is supplied to fuel cell, combustor (5) which carries out diffusive burning using anode off gas, and abnormality inspection device (8) which inspects abnormality of 2nd gas flow path (6) up to combustor via cathode flow path of 2nd oxygen-containing gas supply path and fuel cell.    USE - A fuel cell system.    ADVANTAGE - The system can cope with the problem which arises in combustion of anode off gas of a fuel cell. Size reduction and cost reduction of the fuel cell system are attained.    DETAILED DESCRIPTION - A fuel cell system comprises hydrogen generator which produces hydrogen-containing gas, fuel cell electric-power-generated using hydrogen-containing gas and oxygen-containing gas, 1st oxygen-containing gas supply path into which oxygen-containing gas supplied to hydrogen generator flows, 2nd oxygen-containing gas supply path into which oxygen-containing gas which branches from 1st oxygen-containing gas supply path flows and is supplied to fuel cell, combustor which carries out diffusive burning using anode off gas of fuel cell, and abnormality inspection device which inspects abnormality of 2nd gas flow path up to combustor via cathode flow path of 2nd oxygen-containing gas supply path and fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell system. (Drawing includes non-English language text).    Hydrogen generator (1)    Fuel cell (2)    1st oxygen-containing gas supply path (3)    2nd oxygen-containing gas supply path (4)    Combustor (5)    2nd gas flow path (6)    Abnormality inspection device (8)    Fuel cell system (100)
NOVELTY - Fertilizer (1g) comprises 1.0x 106 mu g/g heat resistant Actinomyces mycelium and thermophilic bacteria. The fertilizer is prepared by fermenting heat resistant Actinomyces mycelium and thermophilic bacteria in a culture medium at pH of 7.5-9.5.    USE - Fertilizer used for growth of plant.    ADVANTAGE - The fertilizer improves yield and quality of agricultural products, such as vegetables and fruit.
NOVELTY - The method involves preparing the electrolytic membrane and membrane electrode assembly (11) containing a catalyst layer. The second fitting portion of one gasket (18) is fitted to first fitting portion of one surface of separator (14). A membrane electrode assembly is temporarily fixed at one surface of separator. The second fitting portion of other gasket (19) is temporarily fixed to the first fitting portion of other surface of the separator. The battery sub-assembly (21) is stacked by performing the process in multiple times.    USE - Method for manufacturing fuel cell stack (claimed) such as direct methanol type fuel cell stack.    ADVANTAGE - The gasket is relatively flexible using the position in which the separator is turned over suitably and the first fitting portion is visually recognized, when the second fitting portion of two gaskets is fitted to the first fitting portion of both surfaces of separator. The reliability of the fitting state of the first fitting portion of separator and the second fitting portion of the gasket is ensured, and the reliability of the gasket is improved. The fuel cell stack is manufactured simply by stacking the battery sub-assembly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the manufacturing process of the battery sub-assembly.    Membrane electrode assembly (11)    Separator (14)    Anode flow path (16)    Gaskets (18,19)    Battery sub-assembly (21)
NOVELTY - In this new utility model relates to one kind of automatic heat PP novel infusion bag, it includes main bag body (1), entrance (2), exit (3), the assistant bag body (4), reaction container (5), liquid pipe (6) and air pipe (8), the assistant bag body (4) is covered on main bag body (1) and outer side, and assistant bag body (4) edge and the main bag body (1) and edge sealing connected with the assistant bag body (4) and is filled between the main bag body (1) with reactant A (10), a reaction container (5) filling with reactant B (11), a reaction container (5) lower part and the assistant bag body (4) and lower part via liquid pipe (6) connected, liquid pipe (6) is also set up with valve A (7), a reaction container (5) top part and the assistant bag body (4) and upper part through air pipe (8) connected, air pipe (8) is also set up with valve B (9). This utility model new advantages and wherein the theory is simple, operation and suitable medicine liquid not easy to be pollute.
NOVELTY - The utility model claims a new one can heating and pressurizing PP of infusion bag, it includes main bag body (1), wherein main bag body (1) is set with entrance (2) and is provided with main bag body (1) and bottom outlet (3), it also comprises assistant bag body (4), a reaction chamber (5) and conduit (6), the assistant bag body (4) top part is covered on the main bag body (1) and outer side, and assistant bag body (4) edge and the main bag body (1) and edge sealing connected with the reaction chamber (5) is equipped with assistant bag body (4) one side of the reaction chamber (5) and assistant bag body (4) between through conduit (6) connected, conduit (6) and is set with valve part (7), and the reaction chamber (5) is set with middle part with diaphragm (10), a diaphragm (10) for reaction chamber (5) divide upper chamber (8) and lower chamber (9). This new utility model advantages is wherein: can control transfusion speed and transfusion, medicine liquid not easy to be pollute and simple operation.
(CN204237572-U)   NOVELTY - Herein describe the used for use in a process of hydrogen cyanide in a waste of a. and b.    DETAILED DESCRIPTION - The present disclosure also provides systems that can operate during production of hydrogen cyanide and reduce the amount of energy or material that is wasted during an Andrussow process.
NOVELTY - The apparatus has tank (2) that contains distilled water, preferably, but not exclusively with potassium hydroxide in solution or sodium hydroxide. A connection is provided to battery of vehicle on which apparatus is installed, or else to some other similar source of electrical energy. A CPU is provided and is interfaced to the pulse generator and is equipped with a pipe (3), which functions as air-flow meter connected to the intake manifold (C) of internal-combustion engine (1) so that air-flow meter subjects to pressure variations that arise in intake manifold.    USE - Apparatus for controlled and instantaneous production of hydrogen to be introduced into intake duct of internal-combustion engine.    ADVANTAGE - The pressure data regarding the manifold detected through air-flow meter are processed by CPU in order to establish the right amount of hydrogen to be produced and introduced into internal-combustion engine. Thus, the CPU is enabled to carry out the functions of management, control, and safety over the entire apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the main components of the apparatus for controlled and instantaneous production of hydrogen to be introduced into intake duct of internal-combustion engine.    Internal-combustion engine (1)    Tank (2)    Pipe (3)    Multi-plate electrolyser (4)    Intake manifold (C)
NOVELTY - The hydrogen generator has compressed filter that is initially expanded to contain portion of the effluent. An effluent storage area (18) volume is increased and reaction area volume is decreased during operation of hydrogen generator. A moveable partition portion separates the effluent storage area from first reactant storage area (14) and reaction area (16). A portion of filter is attached to moveable partition portion. The first reactant is reacted to produce hydrogen gas that is passed through portion of effluent storage area to reach the hydrogen outlet.    USE - Hydrogen generator for fuel cell system.    ADVANTAGE - The volume of hydrogen generator is minimized effectively. The formation of gap between filter and partition portion is prevented. The effluent from bypassing filter by flowing through gap is prevented effectively, such that larger particles in upstream portion are removed effectively. The clogging of filter is prevented reliably. The cost of hydrogen generator is reduced effectively by reusing components even though the hydrogen generator is replaced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the hydrogen generator.    Container (12)    Reactant storage area (14)    Reaction area (16)    Effluent storage area (18)    Filter component (24)    Fluid inlet passage (40)
NOVELTY - The system (1) has a water level judgment part (42) judging water level in a water tank (12), and determines power-consumption load of combustion catalyst heater (34h), that consumes electric power produced in a fuel cell (20). A control part (43) controls the power-consumption load such that the electric power produced in the fuel cell is consumed to make the generated electric power of the fuel cell more than predetermined electric power lower than rated power when the judgment part judges that the water level falls below a predetermined water level in the water tank.    USE - Solid oxide fuel cell system.    ADVANTAGE - The control part controls the power-consumption load such that the electric power produced in the fuel cell is consumed to make the generated electric power of the fuel cell more than predetermined electric power lower than rated power when the judgment part judges that the water level falls below the predetermined water level in the water tank, thus avoiding supply of oxidizing agent gas exceeding flow volume required for electric power generation for cooling of the fuel cell, and hence suppressing decline of water level in the water tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a solid oxide fuel cell system.'(Drawing includes non-English language text)'    Solid oxide fuel cell system (1)    Water tank (12)    Fuel cell (20)    Combustion catalyst heater (34h)    Water level judgment part (42)    Control part (43)
NOVELTY - The method involves forming the electrically conductive region on both sides of the partitioning section (110). The partitioning section is formed inside the injection mold (100). The fluid path is formed between the manifolds and electrically conductive region. The manifolds are separated from each other on the electrically conductive region. The partitioning section formed within the injection mold is removed. An insulation portion is formed between the electrically conductive regions.    USE - Fuel cell manufacturing method using bipolar plate.    ADVANTAGE - The efficiency of the separator manufacture is increased. The process time of the fuel cell is reduced. The material property degradation is reduced. The activation area of the fuel cell separating board is formed. The productivity is increased. The stack power density can be increased. The air leak generated in the boundary face is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell manufacturing method.    Injection mold (100)    Partitioning section (110)    Cover (120)    First insert hole (121)    Second insert hole (122)
NOVELTY - The system has wind-force electricity generation unit (12) that produces electricity using wind force. The solar electric power generation unit (10) receives sunlight to produce electricity. The fuel cell produces and charges battery (19) with electricity generated by power switching unit (16). The electricity produced by the solar electric power generation unit and wind-force electricity generation unit is supplied to load. The sufficient electricity is supplied to hybrid controller (15) according to the insufficient electric energy.    USE - Food garbage disposer hybrid generation system used in apartment house.    ADVANTAGE - The electricity cost of the food waste disposal unit is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the food garbage disposer hybrid generation system.(Drawing includes non-English language text)    Solar electric power generation unit (10)    Wind-force electricity generation unit (12)    Hybrid controller (15)    Power switching unit (16)    Battery (19)
NOVELTY - The method involves storing data regarding a circuit board (13) of operation object in a database server (81). The change of data regarding the circuit board of operation object is reported to a host computer (82). The data stored in the database server are updated based on the received report regarding the change of data regarding the circuit board of operation object. The data of a portion in which a control computer (51) concerns on an update among the data stored in the database server is acquired.    USE - Data update method of circuit-board-related operation system used for mounting electronic component in circuit board such as printed wiring board. Can also be used in data update of setting data for control computer for controlling industrial robot used for performing assembly operation of secondary battery such as solar cell and fuel cell in production line.    ADVANTAGE - The change content of the data regarding the circuit board of operation object between the database server and circuit-board-related operation machine is transmitted reliably. The transmission time is shortened, and the circuit-board-related operation system is provided efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a circuit-board-related operation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the data transmission between database server, host computer, and control computer. (Drawing includes non-English language text)    Control computer (51)    Database server (81)    Host computer (82)    JOB data (91)    Components library (92)
NOVELTY - The apparatus (10) has multiple titanium oxide electrodes (16) which are comprised with an anode and a cathode. A dry cell (18) is provided to apply voltage to titanium oxide electrodes. An UV irradiation unit (20) is provided with ultraviolet-ray induced optical path (20A) for irradiating an UV-ray to titanium oxide electrodes. A control unit (22) is provided to carry out switching control of the polarity of titanium oxide electrode. The titanium oxide electrode and ultraviolet-ray induced optical path are allowed to submerge in water from which hydrogenous water is produced.    USE - Apparatus for manufacturing drinking hydrogenous water, used in house.    ADVANTAGE - The hydrogenous water is manufactured simply at a favorite place. The size reduction of the apparatus is attained, so that the compact hydrogenous water manufacturing apparatus is attained. The generation efficiency of the hydrogen is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the hydrogenous water manufacturing apparatus. (Drawing includes non-English language text)    Hydrogenous water manufacturing apparatus (10)    Titanium oxide electrode (16)    Dry cell (18)    Ultraviolet irradiation unit (20)    Ultraviolet-ray induced optical path (20A)    Control unit (22)
NOVELTY - A high-abundance 13C product low-temperature multi-tower cascade rectification energy-saving device comprises horizontal tower cascade rectifying tower filled with inner plate corrugated filler, screen corrugated filler or saw-toothed corrugated filler, gas phase pipeline (24), liquid phase pipeline (17), condenser (16), rectifying tower reboiler (19), liquid pump, secondary rectifying tower (22) and waste gas discharging pipeline.    USE - High-abundance 13C product low-temperature multi-tower cascade rectification energy-saving device.    ADVANTAGE - The device has low energy consumption, high filler separating efficiency, reliable conveying method, reduced size, increased capacity and reduced production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of high-abundance 13C product low-temperature multi-tower cascade rectification energy-saving device.    Condenser (16)    Liquid phase pipeline (17)    Rectifying tower reboiler (19)    Secondary rectifying tower (22)    Gas phase pipeline (24)
NOVELTY - Vegetable oil reformation involves mixing vegetable oil with water to form an aqueous solution of vegetable oil, and then placing vegetable oil solution into plasma generator through an atomizer. A high voltage is applied to electrodes including center electrode (1) and outer electrode (3) in high-voltage action. The center electrode and the outer electrode promote high-speed rotation of the vegetable oil by using the narrowest point arc plasma generator. The obtained non-thermal arc plasma is reformed to produce a hydrogen-rich gas mixture.    USE - Method for reforming vegetable oil for producing hydrogen (claimed).    ADVANTAGE - The method produces hydrogen gas in a simple and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the vegetable oil reformation method.    Center electrode (1)    Polytetrafluoroethylene layer (2)    Outer electrode (3)    Cylindrical outer wall (4)    Outlet (6)
NOVELTY - Producing hydrogen rich gas mixture involves mixing biological oil and water and then atomizing the obtained material into a plasma generator. The plasma generator is started by applying the high voltage at central electrode (1) and outside electrode (3). The mixture of biological oil and water is kept in between the center electrode and outside electrode and then the obtained material is subjected to quenching process with continuous circulation to produce non-thermal arc plasma. The plasma-induced bio-oil is subjected to reforming chemical reaction to obtain the desired product.    USE - Method for producing hydrogen rich gas mixture (claimed).    ADVANTAGE - The method enables to produce hydrogen rich gas mixture in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a plasma generator.    Central electrode (1)    Outside electrode (3)    Outside wall (4)    Inlet (5)    Outlet (6)
NOVELTY - Preparing wastewater treatment microbial agent involves drying crop straw and then crushing into straw powder with a grinder. The straw powder is added into a fermentation tank and then adding beans cypress and water. The obtained material is stirred at a speed of 500 revolutions per minutes for 30 minutes and then the stirred material is kept for 24 hours to obtain the microorganism nutrient, where the fermentation tank temperature is 70-80 degrees C. The diatomaceous earth and chitosan are crushed into 100-200 meshes particles.    USE - Method for preparing wastewater treatment microbial agent (claimed).    ADVANTAGE - The method enables to prepare wastewater treatment microbial agent in cost-effective manner.    DETAILED DESCRIPTION - Preparing wastewater treatment microbial agent involves drying crop straw and then crushing into straw powder with a grinder. The straw powder is added into a fermentation tank and then adding beans cypress and water. The obtained material is stirred at a speed of 500 revolutions per minutes for 30 minutes and then the stirred material is kept for 24 hours to obtain the microorganism nutrient, where the fermentation tank temperature is 70-80 degrees C. The diatomaceous earth and chitosan are crushed into 100-200 meshes particles. The Enterococcus fecalis, Bacillus licheniformis, Acinetobacter baumannii Rhodococcus, Sphingosine and fluorescent Pseudomonas are cultured and then the cultured material is mixed and then the mixed material is stirred at 30 degrees C for 12 hours. The stirred material is added with diatomaceous earth and chitosan crushed material and then the obtained material is stirred at 100 revolutions per minutes for 3 minutes. The stirred material is dried at 20-22 degrees C to reduce water content to 6-8% to obtain the desired product.
NOVELTY - Production of ethanol involves contacting acetic acid and hydrogen reactor in presence of catalyst comprising binder, and oxide comprising nickel and tin.    USE - Production of ethanol. Uses include but are not limited to pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption, and raw material of ethyl acetate, aldehydes and higher alcohol.    ADVANTAGE - The method enables stable production of ethanol using hydrogenation catalyst which does not require precious metals, with high yield, and enables efficient recycle of catalyst. Need to change the catalyst and reduces reactor down time for continuous processes is reduced.
NOVELTY - Preparing vermicompost leachate involves mixing cattle manure with rabbit manure in molar ratio of 1:1, followed by inoculation of Eisenia fetida to obtain 25 g per kg of the manure mixture. The moisture content of the manure mixture is maintained at 80%. The manure mixture is subjected to fermenter to perform aerobic fermentation at 0.1 volumes of air per minute per volume of batch for 20 days to obtain the finished product.    USE - Method used for preparing vermicompost leachate used for eliminating pathogenic fungi from ornamental garden plants (claimed).    ADVANTAGE - The method enables to prepare vermicompost leachate with good physicochemical and microbiological characteristics effectively eliminates pathogenic fungi from ornamental garden plants, and thus holds major interest in agroindustrial plants.
NOVELTY - Producing hydrogen from organic peroxide comprises providing a steam reformer, providing organic peroxide and water, at least partially decomposing the organic peroxide into decomposition products, reforming the decomposition products and/or organic peroxide in the steam reformer, where decomposition heat of the decomposition products and/or organic peroxide is at least partially used to generate steam.    USE - The hydrogen is useful as a fuel in a fuel cell (claimed).    ADVANTAGE - The method: does not use electricity for steam production since the decomposition heat of peroxy-fuels provides the energy required for steam generation; utilizes excess amount of heat to generate electricity; reduces the production cost of a plant; reduces cost of liquefaction, cooling, and transport; reduces risks of explosion during explosive gas formation, and unavoidable losses occurring during decanting and filling upon delivery of hydrogen from large plants to the respective location can be avoided.    DETAILED DESCRIPTION - INDEPENDENT CLAIM are included for the following    1) a steam reformer for reforming fuel, comprising organic peroxide including a decomposition chamber, which is surrounded by a doubled wall and forms an enclosing chamber, which has fluidic connection with a water supply;    2) Use of an organic peroxide in preparation of synthesis gas.
NOVELTY - Production of pellets involves mixing preliminary ground lignocellulosic plant raw material with binding agent, and pelletizing obtained mixture. 10-20 wt.% Wood bark is used as binding agent. Biologically active compounds of wood bark are extracted by organic solvents.    USE - Production of pellets used as fuel.    ADVANTAGE - The method enables production of pellets having high heating value, bulk density, energy density and attrition resistance, and reduced ash content, and decreases the yield of fine unpelletized biomass.
NOVELTY - Synthesizing ormetoprim comprises (a) carrying out condensation reaction of 4,5-dimethyl-2-methyl-benzaldehyde and 3-methoxy propionitrile in sodium methoxide methanol solution; and (b) adding guanidine hydrochloride into the reaction mixture, and carrying out cyclization reaction.    USE - The method is useful for synthesizing ormetoprim (claimed).    ADVANTAGE - The method is environmentally-friendly, has short reaction period, uses easily obtainable raw materials, is economical, has simple operation and is suitable for large-scale industrialization.
NOVELTY - A sesamin is prepared by smashing sesame, putting into high pressure tank, adding purified water, uniformly pressurizing to 4 kgf/cm2 for 10-15 minutes, restoring atmospheric pressure, filtering to obtain extract, performing aqueous dual-phase extraction in sesame to obtain upper phase and lower phase extracts, performing aqueous dual-phase extraction with 10-20 mass% polyethylene glycol, 5-10 mass% sodium hydroxide, and balance water, desalting upper phase extract, adding diethyl ether to precipitate, and standing in which polyethylene glycol has number average molecular weight of 1000-8000.    USE - Preparation of sesamin.    ADVANTAGE - Process is simple, low cost, short, and environment-friendly and has high extraction rate, and product has improved yield.
NOVELTY - The apparatus has a first chamber and a second chamber receiving and heating a material in an atmosphere with reduced oxygen. A controller regulates oxygen content in the second chamber. A heat treatment chamber is provided with a burner and a syngas inlet to receive syngas from the first chamber and carbon monoxide from the second chamber. The heat treatment chamber is heated with gas, and quenches any volatile organic compounds and long chain hydrocarbons.    USE - Waste processing apparatus.
NOVELTY - Soil composition comprises 20-25 pts. wt. garden soil, 15-20 pts. wt. perlite, 8-15 pts. wt. tree, 10-15 pts. wt. pine needle, 5-10 pts. wt. rice bran, 10-20 pts. wt. urea, 10-15 pts. wt. calcium superphosphate, 5-15 pts. wt. potassium nitrate, 1-5 pts. wt. photosynthetic bacteria, 2-8 pts. wt. nitrogen-fixing bacteria, 1-3 pts. wt. phosphate solubilizing bacteria, and 5-10 pts. wt. plant rhizosphere growth-promoting agent.    USE - The soil composition is useful for planting fruit trees (claimed).    ADVANTAGE - The composition improves water retention effect and fertility of soil, controls insect pests of fruit, and improves yield of fruits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the soil composition, which involves (a) crushing the tree, pine needle and rice bran, and adding crushed components to a fermentation tank, (b) adding 200-300 times deionized water to the photosynthetic bacteria, nitrogen-fixing bacteria, phosphate solubilizing bacteria and plant rhizosphere growth-promoting agent, adding obtained mixture to the fermentation tank, stirring the mixture, covering the mixture using plastic film, fermenting the mixture for 2-5 days, and exposing fermented product to sun for 2-3 days, (c) crushing the garden soil, sieving the garden soil using sieve having 200 mesh size, uniformly mixing the gardens soil with perlite, stirring obtained mixture, adding the urea, calcium superphosphate and potassium nitrate to the mixture, and stirring the mixture, and (d) mixing products obtained in steps (b) and (c), and uniformly stirring obtained product.
NOVELTY - Producing soil modifying agent involves utilizing 15 pts. wt. humic acid, 65 pts. wt. cattle and sheep dung, 30 pts. wt. aqueous solution of potassium hydroxide, 0.01 pts. wt. catalyst, 5 pts. wt. amino acid, 5 pts. wt. dimethylurea, 1 pts. wt. oxalic acid, 3 pts. wt. ammonium sulfate, 3 pts. wt. phosphogypsum, 4 pts. wt. trace element, 0.5 pts. wt. polyacrylamide, 0.5 pts. wt. polyvinyl alcohol, 3 pts. wt. potassium sulfate, 2 pts. wt. brown sugar, 0.1 pts. wt. phosphorus and potassium solution, 0.1 pts. wt. biological enzyme and 0.1 pts. wt. composite bacteria.    USE - Method for producing soil modifying agent (claimed).    ADVANTAGE - The method enables to produce soil modifying agent in a simple and cost-effective manner. The soil modifying agent increases organic matter in soil, and improves soil micro-environment.    DETAILED DESCRIPTION - Producing soil modifying agent involves utilizing 15 pts. wt. humic acid, 65 pts. wt. cattle and sheep dung, 30 pts. wt. aqueous solution of potassium hydroxide, 0.01 pts. wt. catalyst, 5 pts. wt. amino acid, 5 pts. wt. dimethylurea, 1 pts. wt. oxalic acid, 3 pts. wt. ammonium sulfate, 3 pts. wt. phosphogypsum, 4 pts. wt. trace element, 0.5 pts. wt. polyacrylamide, 0.5 pts. wt. polyvinyl alcohol, 3 pts. wt. potassium sulfate, 2 pts. wt. brown sugar, 0.1 pts. wt. phosphorus and potassium solution, 0.1 pts. wt. biological enzyme and 0.1 pts. wt. composite bacteria. Humate, cattle and sheep dung, catalyst, trace element, phosphorus and potassium solution and potassium sulfate, aqueous solution of potassium hydroxide are mixed with Bacillus and silicate bacteria at 150-170 degrees C for 2 hours in a reaction kettle to obtain organic liquid. Organic liquid is decompressed and stirred at normal pressure for 20 minutes, and then remaining components are mixed at 40-50 degrees C for 30 minutes. biological enzyme is mixed with obtained product, and then stirred for 30 minutes.
NOVELTY - Natural organic fertilizer comprises 15-35 wt.% peanut shell, 10-25 wt.% bean residues, 20-40 wt.% soil carbon, 20-30 wt.% chicken manure and 2-5 wt.% effective microorganism (EM).    USE - As natural organic fertilizer.    ADVANTAGE - The fertilizer is prepared cost-effectively, convenient to use, and rich in lipid, protein and organic substances, and has high durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the natural organic fertilizer, which involves (a) crushing the peanut shell and bean residues, respectively, (b) fermenting the soil carbon and chicken manure, respectively, and (c) uniformly mixing products obtained in steps (a) and (b) to obtain product.
NOVELTY - A rich silicon biocarbon organofertilizer is prepared by taking rice husk, rice bran and Bacillus subtilis, stir mixing, adding water, fermenting, adding biocarbon and effective microorganisms, mixing uniformly, adding water, fermenting, uniformly spraying molasses, mixing uniformly, continuously stirring to ferment, extruding and granulating, drying, cooling, and sieving.    USE - Method for preparing rich silicon biocarbon organofertilizer (claimed).    ADVANTAGE - The method uses biocarbon with high silicon content.    DETAILED DESCRIPTION - A rich silicon biocarbon organofertilizer is prepared by taking 80-90 pts. wt. rice husk, 10-20 pts. wt. rice bran and 0.2-0.4 pt. wt. Bacillus subtilis, stir mixing to obtain mixed material, adding water to water content of 60-70%, fermenting for 5-7 days, fermenting at 40 degrees C, adding biocarbon and effective microorganisms, mixing uniformly, adding water to water content of 40-50%, fermenting for 5-7 days in summer and autumn season and for 10-15 days in winter, uniformly spraying molasses, mixing uniformly, continuously stirring to ferment for 2-5 days, extruding and granulating, drying, cooling, and sieving.
NOVELTY - Preparing foliar fertilizer involves boiling soybean for 20 minutes and then crushing to obtain soybean liquid. The soybean liquid is filtered and then dried to obtain soybean powder. Red sugar, rice vinegar, enzyme and bacteria are added into soybean powder and then fermented for 5 days to obtain fermentation material. The fermentation material is dried and then soaked in brown sugar solution for 20 days to obtain the product.    USE - Method for preparing foliar fertilizer (claimed).    ADVANTAGE - The method enables to prepare foliar fertilizer in a simple and cost-effective manner.
NOVELTY - An organic material ferment recycling processing equipment includes machine, deodorizer (20), ice water machine, fermentation box, fermenting room (131), solid organic fertilizer discharge port, tank body, feeding port, discharging transition port, spiral material conveying mechanism (133), solid organic fertilizer material (141), heating device, gas and entrance discharge port, air cooling condensing tank, activated carbon absorbing tank, pipeline, deodorization box body, gas entrance and exit, air filter tank, exhaust device and condensing liquid collection pipeline.    USE - Organic material ferment recycling processing equipment.    DETAILED DESCRIPTION - An organic material ferment recycling processing equipment comprises machine, deodorizer (20), ice water machine, fermentation box, fermenting room (131), solid organic fertilizer discharge port, tank body, feeding port, discharging transition port, spiral material conveying mechanism (133), solid organic fertilizer material (141), heating device, gas and entrance discharge port, air cooling condensing tank, activated carbon absorbing tank, pipeline, deodorization box body, gas entrance and exit, air filter tank, exhaust device, condensing liquid collection pipeline, liquid organic fertilizer discharging tube (251), machine main body, water pump, water pipeline, return water pipeline and condensing pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic material ferment recycling processing equipment.    Deodorizer (20)    Fermenting room (131)    Spiral material conveying mechanism (133)    Solid organic fertilizer material (141)    Liquid organic fertilizer discharging tube (251)
NOVELTY - Fertilizer comprises 50-60 pts. wt. potassium dihydrogen phosphate, 12-18 pts. wt. amino acid mixture, 10-15 pts. wt. sodium humate, 8-11 pts. wt. glutamine and 8-10 pts. wt. water.    USE - Fertilizer used for cultivating Coilia nasus in pond (claimed).    ADVANTAGE - The fertilizer is prepared in a simple and eco-friendly manner and easy to use, and promotes growth of fish by cultivating Coilia nasus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves mixing raw components uniformly, and then filling into container.
NOVELTY - Making (M1) hydrocarbons having more than 2C, comprises: introducing a chlorine stream (12) and methane stream (10) to first reaction zone (2) comprising metal oxide catalyst; converting the metal oxide to metal chloride and reacting methane to form a product comprising hydrocarbon and carbon dioxide, where the hydrocarbon comprises at least one of ethane and ethane; introducing the metal chloride to second reaction zone (4); introducing oxygen source to second reaction zone to convert the metal chloride to metal oxide and chlorine; and directing the metal oxide back to first reaction zone.    USE - The process is useful for conversion of methane to hydrocarbons having more than 2C, including ethane and vinyl chloride (claimed).    ADVANTAGE - The process: provides the selectivity for ethene of greater than or equal to 70% (claimed); and regenerates the metal oxide catalyst by adding oxygen source and reduces the methane combustion due to oxygen by carrying out the processes in two different zones.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for    (1) making (M2) ethane, comprising introducing only a chlorine stream and a methane stream to a metal oxide catalyst to form the ethane and carbon dioxide, where the chlorine stream and the methane stream each comprise less than 1 vol.% oxygen, and metal oxide converts to metal chloride, and separately converting the metal chloride back to metal oxide with oxygen from an oxygen source, where chlorine gas is produced; and    (2) making (M3) vinyl chloride monomer, comprising forming the ethene and the chlorine gas, reacting at least a portion of the chlorine gas and the ethene to form the vinyl chloride monomer.    DESCRIPTION OF DRAWING(S) - The figure illustrates the process for the conversion of methane to more than 2C hydrocarbons.    First reaction zone (2)    Second reaction zone (4)    Methane stream (10)    Chlorine stream (12)    Oxygen stream (20)
NOVELTY - Preparing organic compound fertilizer particles, comprises (i) crushing crop stalks and animal feces, and naturally fermenting the materials by adding into a biogas tank, to obtain biogas slurry and biogas residue, and mixing biogas slurry with crushed crop straw, and stacking biogas residue to carry out natural fermentation, and turning up and down while fermenting at 40-70 degrees C; and (ii) reducing the fermentation temperature at 25 degrees C, until the moisture content reaches 15-25%, decomposing manure, adding fertilizer, urea and potassium chloride and calcium superphosphate, and mixing.    USE - The method is useful for preparing organic compound fertilizer particles (claimed).    ADVANTAGE - The method is simple, and economical; has rapid effect; saves device cost by 70%; increases food production; and promotes virtuous cycle of ecological agriculture.    DETAILED DESCRIPTION - Preparing organic compound fertilizer particles, comprises (i) crushing crop stalks and animal feces, and naturally fermenting the materials by adding into a biogas tank, to obtain biogas slurry and biogas residue, and mixing biogas slurry with crushed crop straw under in-situ conditions, and stacking biogas residue to carry out natural fermentation, and turning up and down while fermenting at 40-70 degrees C; and (ii) reducing the fermentation temperature at 25 degrees C, until the moisture content reaches 15-25%, decomposing manure having pH of 6-7, adding 40% fertilizer, 20% urea and 15% potassium chloride and 25% calcium superphosphate, uniformly mixing while stirring, and adding the material into a screw extruder, to obtain the final product.
NOVELTY - The gasifier has a thermostat and accessories that are provided with complete automation. The gasifier main portion is provided with a reactor, two tar trap boxes, and wet gas filtration cylinder. The best quality substitute gas is produced for internal combustion engines.    USE - Automatic rice hull gasifier.    ADVANTAGE - The increasing coast and use of industrial fuel by producing gas mainly consists of hydrogen and carbon monoxide by-product of burnt rice husk is reduced effectively. The gasifier is provided with complete mechanical automation. Since the thermal sensors, alarms, water filtration system and smart waste disposal are provided, the operation is improved effectively. The best quality substitute gas is produced for internal combustion engines.
NOVELTY - Cell (c1) that recombinantly expresses: (a) a gene encoding a thiolase; (b) a gene encoding an acetoacetyl-co-enzyme A (CoA) reductase; (c) a gene encoding an acyl dehydratase; (d) a gene encoding an enoyl-CoA reductase; and (e) a gene encoding a carboxylic acid reductase, is new.    USE - The cell is useful for producing a branched medium-chain alcohol including 4-methyl-1-pentanol (claimed), which is useful as a liquid fuel.    ADVANTAGE - The cell: provides the 4-methyl-1-pentanol, which exhibits high purity and yield, is miscible with many organic solvents, and is a viable liquid fuel replacement for gasoline with high energy density and branches, hence improves the octane rating of the fuel; and reduces the formation of isobutanol byproduct.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a cell culture or supernatant collected from culturing at least one of the cell(s) (c1), where the cell culture or supernatant optionally contains at least 10 mg/l 4-methyl-1-pentanol;    (2) producing (m1) the cell culture, comprising culturing the cell (c1) in cell culture medium, where optionally glucose and/or isobutyrate are added to the cell culture medium;    (3) producing (m2) 4-methyl-1-pentanol, comprising culturing the cells (c1) to produce a cell culture or supernatant containing 4-methyl-1-pentanol, where optionally the 4-methyl-1-pentanol is further purified from the cell culture or supernatant;    (4) a method (m3) of recombinantly expressing the genes (a)-(e) as above per se in the cell (c1); and    (5) a cell (c2) recombinantly expressing: a module that condenses acetyl-CoA and isobutyryl CoA and reduces the product to form 4-methyl valeryl-CoA; and a module that reduces 4-methyl valerate to 4-methyl-1-pentanol.
NOVELTY - Production of ethanol involves reacting hydrogen feed stream with an acetic acid feed stream in reactor operated in presence of a catalyst to form ethanol mixture, separating vapor stream from the ethanol mixture and liquid stream from ethanol mixture, recovering ethanol from the liquid stream, combining fresh hydrogen stream and vapor stream to form hydrogen feed stream, and monitoring carbon monoxide concentration of fresh hydrogen feed stream and adjusting temperature in reactor in response to carbon monoxide concentration of the fresh hydrogen feed stream.    USE - Production of ethanol. Uses include but are not limited to fuels, solvents, chemical feedstocks, pharmaceutical products, cleansers, sanitizers, solvent for toiletry and cosmetic preparations, detergents, disinfectants, coatings, inks, etc.    ADVANTAGE - The method enables efficient production of ethanol with excellent productivity.    DETAILED DESCRIPTION - Production of ethanol involves reacting hydrogen feed stream with an acetic acid feed stream in a reactor operated in the presence of a catalyst to form an ethanol mixture, separating a vapor stream from the ethanol mixture and a liquid stream from the ethanol mixture, in which the vapor stream has a steady state concentration of carbon monoxide, recovering ethanol from the liquid stream, combining a fresh hydrogen stream and the vapor stream to form the hydrogen feed stream, and monitoring carbon monoxide concentration of the fresh hydrogen feed stream and adjusting temperature in the reactor in response to the carbon monoxide concentration of the fresh hydrogen feed stream.
NOVELTY - Composition (C1) for fuel blending, comprises: isobutanol; an octane improving component; and a vapor pressure adjustment component.    USE - The composition is useful to produce a fuel blend (claimed), which is useful in an automotive engine.    ADVANTAGE - The composition: provides the fuel blend having an octane rating of at least 70-120, an anti-knock index of at least 70-120, a vapor pressure of less than or equal to 15 psi, preferably less than or equal to 1 psi, and a driveability index of less than or equal to 1000-1400?F (claimed), and exhibiting improved distillation properties and kinematic viscosity; serves as alternatives to ethanol-containing fuel blends; and minimizes an air pollution caused by exhaust emissions of an automotive vehicle having a combustion engine.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a composition (C2) for fuel blending, comprising: 60-90 vol.% of isobutanol; 5-35 vol.% of toluene; and 5-20 vol.% of n-butane; and    (2) a fuel blend comprising: the isobutanol; the octane improving component; the vapor pressure adjustment component; and a gasoline and/or a gasoline blend stock, where the gasoline and/or gasoline blend stock is formulated for the addition of ethanol.
NOVELTY - A thermal cracking additive composition comprises 40-85 wt.% alumina, 5-20 wt.% colloidal silica including 20-45 wt.% silica, and 0.1-13 wt.% phosphate compound. The alumina comprises boehmite alumina and 2-40 wt.% dispersible alumina.    USE - Thermal cracking additive composition is used for reducing coke yield in Delayed coking process (all claimed).    ADVANTAGE - The thermal cracking additive composition decreases the coke yield, and increases yield of liquids and/or gaseous products.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of additive composition, which involves treating boehmite alumina with demineralized water to obtain boehmite slurry, treating boehmite slurry with phosphate compound to obtain phosphate-treated boehmite slurry, gelling dispersible alumina employing mineral or organic acid, adding colloidal silica to obtained product at pH of 1-5, adding the phosphate-treated boehmite slurry to the obtained product, spray-drying the obtained product, and calcining the spray-dried particles to obtain the additive composition;    (2) process for reducing coke yield in Delayed Coking process, which involves contacting a feedstock with the additive in a coke drum, and separating the cracked product to obtain different fractions; and    (3) use of the additive composition for reducing coke yield in Delayed coking process, in which the reduction in coke yield is 1-5 wt.% with respect to base case.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining Delayed Coking process.    Residual hydrocarbon feedstock (1)    Fractionater (3)    Coker heater (7)    Vapor liquid mixture (8)    Coking drum (9)
NOVELTY - A fresh tobacco leaf waste gas is produced by collecting waste fresh tobacco leaf raw material, cutting by cutter to length of 5-10 cm, subjecting waste fresh tobacco leaves and excrement for fermentation to control nitrogen content, stacking waste fresh tobacco leaves and excrement in anaerobic reactor until 85% of reactor volume is occupied, piling for 2-4 days, inoculating with biogas, adding fresh water, controlling concentration of total solids (TS) to 2-6%, adding alkali, controlling pH to 6.5-7.5, sealing reactor, and placing in storage device at room temperature under fermentation gas.    USE - Production of fresh tobacco leaf waste gas.    ADVANTAGE - Process has no pollution and high marsh gas production rate and reduces cost.    DETAILED DESCRIPTION - A fresh tobacco leaf waste gas is produced by collecting waste fresh tobacco leaf raw material, cutting by cutter to length of 5-10 cm, subjecting waste fresh tobacco leaves and excrement for fermentation to control nitrogen content, stacking waste fresh tobacco leaves and excrement in anaerobic reactor until 85% of anaerobic reactor volume is occupied, piling for 2-4 days under natural condition, inoculating with biogas in amount of 10-15% of anaerobic reactor volume, adding fresh water, controlling concentration of total solids (TS) to 2-6%, adding alkali, controlling pH to 6.5-7.5, sealing anaerobic reactor, and placing in storage device at room temperature under fermentation gas.
NOVELTY - A short chain fatty acid is prepared by using sludge as fermentation substrate, adding sodium nitrite in fermenting substrate, acidic pretreating, and anaerobic fermenting.    USE - Preparation of short chain fatty acid (claimed).    ADVANTAGE - The preparation reduces sludge and organic pollution, increases fatty acid content and hydrolysis rate of sludge, shortens sludge fermentation time, optimizes existing sludge treatment system, and has high product yield and low energy consumption and operation cost.
NOVELTY - Composite fertilizer comprises 20-30 pts. wt. Chinese medicine fermentation product, 5-10 pts. wt. urea, 5-10 pts. wt. potassium chloride, 2-4 pts. wt. diammonium phosphate, 20-30 pts. wt. animal manure, 3-6 pts. wt. humic acid, 0.5-1 pts. wt. micro-nutrient fertilizers and 0.01-0.02 pts. wt. plant growth agents.    USE - The composite fertilizer is useful for promoting wheat growth; and killing pests, and bacteria.    ADVANTAGE - The composite fertilizer is rich in nutrient substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the composite fertilizer, comprising (i) taking Coriaria sinica Maxim., radix sophorae flavescentis, radix bupleuri, Angelica, radix rehmanniae, Aconitum, Eucommia ulmoides, Forsythia, immature bitter orange, Cassia bark and Chinese yam, and crushing into 0.2 mm powder, then boiling for 3 hours by adding water in an amount of 3 times, and naturally cooling; (ii) uniform stirring urea, potassium chloride and diammonium phosphate with the product obtained in the step (i), and evaporating water under reduced pressure; (iii) subjecting the product of the step (ii) to aerobic fermentation, where the oxygen content is 10%, and fermenting at less than 70 degrees C for 15-25 days; (iv) mixing chicken manure and cow dung, and sealing, and packing while fermenting for 40-60 days; and (v) uniformly mixing the obtained product with the remaining raw materials.
NOVELTY - Preparation of tea tree fertilizer includes mixing animal manure, plant straw, wheat bran and soybean residue, and fermenting to obtain fermented substance; feeding into miller, crushing, indoor drying, adding urea, calcium superphosphate, diammonium phosphate, potassium dihydrogen phosphate, magnesium sulfate, zinc sulfate and trace elements, and mixing; and drying, adding effective microorganism, mixing, granulating, low-temperature drying, sieving, and packaging.    USE - Method for preparation of tea tree fertilizer (claimed).    ADVANTAGE - The fertilizer is suitable for large-scale industrial production, can meet nutrition requirement of tea tree, and it has reasonable component proportion, simple process and low cost.    DETAILED DESCRIPTION - Preparation of tea tree fertilizer comprises mixing 80-100 pts. wt. animal manure, 40-50 pts. wt. plant straw, 40-50 pts. wt. wheat bran and 20-30 pts. wt. soybean residue, and fermenting to obtain fermented substance; feeding into miller, crushing, indoor drying until moisture content is below 50%, adding 60-80 pts. wt. urea, 50-60 pts. wt. calcium superphosphate, 20-30 pts. wt. diammonium phosphate, 30-40 pts. wt. potassium dihydrogen phosphate, 6-10 pts. wt. magnesium sulfate, 4-8 pts. wt. zinc sulfate and 3-4 pts. wt. trace elements, and mixing; and drying, adding 3-4 pts. wt. effective microorganism, mixing, adding into granulator, granulating, low-temperature drying, sieving, and packaging.
NOVELTY - Preparing silver indium selenide nano-crystal comprises (i) taking silver nitrate, indium chloride and/or indium chloride tetrahydrate, selenium dioxide, polyvinylpyrrolidone and dimethylformamide as raw materials, mixing and uniformly stirring to obtain precursor solution; and (ii) placing the precursor solution in a high-pressure reaction kettle, reacting at constant temperature of 160-220 degrees C for 3-20 hours, centrifuging the reaction solution to collect solid, washing the resulting solid using a solvent, and drying to obtain silver indium selenide nanometer crystal.    USE - The nano-crystal is useful in biological medicine and aqueous phase photocatalysis field.    ADVANTAGE - The method: is simple and environmentally friendly; utilizes economical raw materials; has short period and good repeatability; and produces the nano-crystals, which can be dispersed in the aqueous phase.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for silver indium selenide nano-crystal prepared by the above mentioned method, where space group is Pna21 metastable orthorhombic system and is soluble in water.
NOVELTY - A municipal high concentrated sludge coal slurry is prepared by quenching and tempering sludge source with sludge conditioning agent, standing for 20-60 minutes, gravity dehydrating, discharging supernatant liquid to obtain concentrated sludge, mixing concentrated sludge with coal and additive at certain mixing ratio in which solid slurry content of concentrated sludge and coal is 10-18 wt.%, and ball-milling to less than or equal to 0.1 mm particle diameter in which 70-80% of product has less than or equal to 75 mu m particle diameter.    USE - Preparation of municipal high concentrated sludge coal slurry (claimed).    ADVANTAGE - The preparation improves sludge dehydration performance, increase sludge heat value and sludge depth, has no pre-drying sludge, reduces cost, protects environment, and effectively uses sludge resource.
NOVELTY - Activated sludge is pre-processed by irradiating gamma -ray with intensity of 7-25 kGy to activated sludge for 8-12 s to obtain gamma -ray irradiated sludge, ultrasonic-wave processing gamma -ray irradiated sludge using ultrasonic wave energy density of 1-1.2 W/ml and power of 20-40 kHz for 20-60 minutes to obtain sludge, adjusting pH of sludge to 9-12, and anaerobically fermenting at 25-40 degrees C for 2-6 days.    USE - Combined pre-processing of activated sludge for production of short chain fatty acids (claimed).    ADVANTAGE - The activated sludge gamma -ray irradiation and ultrasonic wave pre-processing can increase protein, polysaccharide, and sludge organic matter dissolved in water to provide rich water-soluble acid fermented organic sludge matrix, increase rate of acid sludge, shorten time of sludge anaerobic fermentation, improve existing sludge treatment system, saves energy, and reduces operation cost. Increase of residual sludge biological production yield of short chain fatty acid is increased. Anaerobic fermentation can be used to supplement lack of carbon sludge or for production of methane and other clean energy sources, minimizing the degradation of organic matter in sludge to achieve sludge reduction, stabilization, recycling, and reduction of sludge organic pollution to the environment.
NOVELTY - Manufacture of organic fertilizer comprises taking 65-75 pts. wt. straw, swelling to obtain expanded straw, mixing with 0.1-0.2 pt. wt. decomposing inoculant and 50-60 pts. wt. water, forming mixed liquid, mixing with expanded straw, forming mixed material and fermenting for 6-8 days.    USE - Method for manufacture of organic fertilizer (claimed).    ADVANTAGE - The fertilizer increases straw decomposition and contact area, shortens decomposition period and reduces production cost.
NOVELTY - Production of wine lees pig manure organic fertilizer comprises drying pig manure by drying agent and dehydrating by dehydrating machine, taking strip stack, composting pig manure, curing, adding wine lees, mixing and fermenting; adding fungus dreg and protease, uniformly mixing and scattering on stack surface; adding filler comprising wheat straw powder, bean leaf powder, grass powder, leaves powder, peat and grass ash, adding decomposing microbial inoculum and corn flour and fermenting while uniformly stirring; and turning, removing strip stack and adding protease, urease and phosphatase.    USE - Method for producing wine lees pig manure organic fertilizer (claimed).    ADVANTAGE - The method reduces environmental pollution and improves economical benefit of farmers.    DETAILED DESCRIPTION - Production of wine lees pig manure organic fertilizer comprises:    (A) drying pig manure by drying agent and dehydrating by dehydrating machine to water content of 20%;    (B) taking strip stack having width of 4 m, height of 2 m and any length, composting pig manure, curing at higher than 15 degrees C, adding wine lees, mixing and fermenting;    (C) adding 200 kg fungus dreg and 100 g protease, uniformly mixing and scattering on stack surface;    (D) adding filler comprising wheat straw powder, bean leaf powder, grass powder, leaves powder, peat and grass ash, adding decomposing microbial inoculum and corn flour and fermenting while uniformly stirring at 60 degrees C; and    (E) turning at interval of 4-5 days, removing strip stack and adding protease, urease and phosphatase.
NOVELTY - A walnut functional organic-inorganic composite fertilizer comprises 40-50 pts. wt. cattle manure fermentation component, 20-30 pts. wt. vegetable slag fermentation component, 10-18 pts. wt. urea, 3-10 pts. wt. potassium sulfate, 8-9.5 pts. wt. calcium magnesium phosphate fertilizer, 0.1-0.4 pt. wt. borax and 0.1-0.4 pt. wt. zinc sulfate.    USE - Walnut functional organic-inorganic composite fertilizer.    ADVANTAGE - The fertilizer has easy-to-obtain materials and low cost. It solves the problem about environmental pollution of cattle manure and vegetable slag waste, and increases yield. Its nutrients are more absorbed to improve soil fertility. The method has simple production technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of walnut functional organic-inorganic composite fertilizer comprising taking cattle manure or vegetable slag, uniformly mixing with 0.3-0.5% fermentation bacteria, stacking for 15-25 days, expanding, drying to water content of less than 10% to obtain cattle manure fermentation component or vegetable slag fermentation component, weighing urea, potassium sulfate, calcium magnesium phosphate fertilizer, borax and zinc sulfate, crushing, sieving and uniformly mixing with cattle manure fermentation component and vegetable slag fermentation component.
NOVELTY - Mulberry fertilizer comprises 80-100 pts. wt. fermented livestock manure, 30-50 pts. wt. humic acid, 60-80 pts. wt. silkworm dropping, 20-30 pts. wt. weathered coal, 1-3 pts. wt. boron fertilizer, 3-5 pts. wt. ferrous sulfate, 5-10 pts. wt. ammonium molybdate, 30-50 pts. wt. canal mud, 5-10 pts. wt. effective microorganisms (EM) inoculum, and 50-80 pts. wt. tea waste residue.    USE - Used as mulberry fertilizer.    ADVANTAGE - The mulberry fertilizer: is nutritional efficient; can fully meets growing requirements of the mulberry; is conducive to the absorption of mulberry; prevents soil compaction; and greatly increases mulberry leaves.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the mulberry fertilizer, comprising (i) crushing the canal mud, weathered coal and tea waste residue, and mixing to obtain nutrient river mud; (ii) uniformly mixing the fermented livestock manure, silkworm dropping and EM microbial inoculum, and fermenting at temperature of 25-35 degrees C for 3-5 days to obtain fermented substance; (iii) mixing the nutrient river mud, fermented substance, humic acid, boric fertilizer, ferrous sulfate and ammonium molybdate, and uniformly stirring to obtain fertilizer raw material; and (iv) sterilizing the fertilizer raw material, and drying to obtain the product.
NOVELTY - A biological organic fertilizer comprises 300-500 pts. wt. rice bran, 500-1000 pts. wt. straw, 100-200 pts. wt. soybean residue, 1-10 pts. wt. effective microorganism microbial inoculum, 5-10 pts. wt. brown sugar, 50-100 pts. wt. urea, 100-150 pts. wt. calcium superphosphate, 20-100 pts. wt. magnesium sulfate, 20-100 pts. wt. potassium sulfate, 50-100 pts. wt. ammonium sulfate, and 300-600 pts. wt. water.    USE - Biological organic fertilizer used for promoting growth of crops.    ADVANTAGE - The fertilizer has comprehensive nutrition, no bacteria, parasite eggs residues, and high safety on human, animals, and crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fertilizer comprising taking weighed raw materials, mixing, pile stacking, ventilating, and covering; stack fermenting at 40-50 degrees C, turning, and pile stacking; fermenting at 55-60 degrees C, turning, and stacking; and fermenting for 1-5 days and drying.
NOVELTY - Preparing fertilizer for potato, by mixing finely chopped plant stalks and soybean meal, peat and animal excrement in predetermined weight proportions, fermenting obtained mixture, mixing obtained fermented product, urea, calcium superphosphate, diammonium phosphate, potassium chloride, borax, manganese sulfate, zinc sulfate and silicates in predetermined weight proportions, crushing obtained mixture, stirring crushed product uniformly to obtain powdered fertilizer, drying the powdered fertilizer, and granulating dried product using granulator.    USE - The method is useful for preparing fertilizer which is used for cultivation of potato (claimed).    ADVANTAGE - The method enables preparation of fertilizer that provides all essential nutrients including nitrogen, phosphorus, potassium, manganese, zinc and silicon, required for growth and development of potato.    DETAILED DESCRIPTION - Method for preparing fertilizer for potato, involves (a) mixing finely chopped plant stalks and soybean meal, peat and animal excrement in predetermined weight proportions, and fermenting obtained mixture for 50-60 days, (b) mixing obtained fermented product, urea, calcium superphosphate, diammonium phosphate, potassium chloride, borax, manganese sulfate, zinc sulfate and silicates in predetermined weight proportions, crushing obtained mixture, and stirring crushed product uniformly to obtain powdered fertilizer, and (c) drying the powdered fertilizer at 65-75 degrees C, and granulating dried product using granulator to obtain granular fertilizer.
NOVELTY - Preparation of vegetable biological fertilizer comprises taking 20-30 pts. wt. biogas residue, 20-30 pts. wt. rapeseed cake, 10-20 pts. wt. animal manure and 15-20 pts. wt. rice bran, stirring, adding 1-3 pts. wt. effective microorganism microbial inoculum, mixing, adding into fermentation tank, fermenting, pouring 5-10 pts. wt. sodium nitrate, 5-10 pts. wt. calcium nitrate, 10-15 pts. wt. ammonium hydrogen phosphate, 10-15 pts. wt. potassium chloride, 3-5 pts. wt. borax and 3-5 pts. wt. Chinese medicine composition, stirring, fermenting, taking out, drying, crushing and granulating.    USE - Method for preparing vegetable biological fertilizer (claimed).    DETAILED DESCRIPTION - Preparation of vegetable biological fertilizer comprises taking 20-30 pts. wt. biogas residue, 20-30 pts. wt. rapeseed cake, 10-20 pts. wt. animal manure and 15-20 pts. wt. rice bran, uniformly stirring by stirrer, adding 1-3 pts. wt. effective microorganism microbial inoculum, uniformly mixing, adding into fermentation tank, fermenting for 20-25 days, pouring 5-10 pts. wt. sodium nitrate, 5-10 pts. wt. calcium nitrate, 10-15 pts. wt. ammonium hydrogen phosphate, 10-15 pts. wt. potassium chloride, 3-5 pts. wt. borax and 3-5 pts. wt. Chinese medicine composition, uniformly stirring, continuously fermenting for 5-7 days, taking out, drying, crushing and granulating. An INDEPENDENT CLAIM is included for preparation of Chinese medicine composition comprising soaking tuber pinellia, Euphorbia, dandelion, Bidens and radix glycyrrhizae in water for 3 hours, boiling at low heat for 3-4 hours and pouring out medicine liquid.
NOVELTY - A selenium-enriched chitosan microbial fertilizer comprises sodium selenite, chitosan hydrolyzate, composite trace elements, potassium dihydrogen phosphate, urea, peptone, yeast powder, sodium chloride, sodium hydroxide, sodium nitrate, ammonium chloride, potassium phosphate, beef extract, glucose, starch, calcium carbonate, amino acid, potassium nitrate, ferrous sulfate, magnesium sulfate, sodium citrate, enzyme and mixed bacterial liquid.    USE - Selenium-enriched chitosan microbial fertilizer (claimed).    ADVANTAGE - The economic fertilizer has excellent moisture retention property and slow-release fertilizer effect, and increases crop yield by 10-15%.    DETAILED DESCRIPTION - A selenium-enriched chitosan microbial fertilizer comprises 8-15 pts. wt. sodium selenite, 55-75 pts. wt. chitosan hydrolyzate, 5-15 pts. wt. composite trace elements, 8-20 pts. wt. potassium dihydrogen phosphate, 10-25 pts. wt. urea, 8-20 pts. wt. peptone, 4-10 pts. wt. yeast powder, 8-20 pts. wt. or 10-25 pts. wt. sodium chloride, 8-15 pts. wt. sodium hydroxide, 4-10 pts. wt. sodium nitrate, 4-10 pts. wt. ammonium chloride, 8-20 pts. wt. potassium phosphate, 4-10 pts. wt. beef extract, 10-25 pts. wt. glucose, 10-25 pts. wt. starch, 8-20 pts. wt. calcium carbonate, 10-25 pts. wt. amino acid, 2-6 pts. wt. potassium nitrate, 2-6 pts. wt. ferrous sulfate, 10-25 pts. wt. magnesium sulfate, 25-40 pts. wt. sodium citrate, 10-25 pts. wt. enzyme and 800-848 pts. wt. mixed bacterial liquid. An INDEPENDENT CLAIM is included for preparation of selenium-enriched chitosan microbial fertilizer.
NOVELTY - Compound microbial fertilizer comprises 0.2-2 pts. wt. biological bacteria, 5-58 pts. wt. high humic acid containing peat, 2-6 pts. wt. trace elements, 2-10 pts. wt. conditioner and 6-45 wt.% inorganic fertilizers rich in nitrogen, phosphorus and potassium nutrients.    USE - Compound microbial fertilizer used for maintaining soil for cultivating pomegranate fruit.    ADVANTAGE - The compound microbial fertilizer is eco-friendly, and ensures increased fertilizer utilization rate and reduced production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound microbial fertilizer, which involves:    (A) weighing and sieving raw materials to obtain powder;    (B) mixing Bacillus powders and high humic acid containing peat to obtain fertilizer that is mixed with trace elements and conditioning agent to obtain another mixture;    (C) granulating obtained mixture using cold pressing with pelleting machine into compound microbial fertilizer granule material;    (D) sieving obtained materials to obtain product of desired size; and    (E) packaging product.
NOVELTY - An acid is added to mother liquid containing D-(+)-malic acid obtained after resolution of zopiclone, and pH is controlled to 1-3. Saturated ammonium sulfate is added to the obtained solution and the mixture is extracted using ethyl acetate. The obtained extract is concentrated to a volume of 1/10-1/8, crystallized by cooling and filtered to obtain D-(+)-malic acid.    USE - Recovery of D-(+)-malic acid used as zopiclone resolving agent.    ADVANTAGE - The recovery method produces D-(+)-malic acid with high optical purity with recovery rate of 90% by a one-step process, economically, with reduced energy consumption and with improved productivity.
NOVELTY - Preparing 2,4-D-dimethylamine salt comprises dissolving 2,4-D original drug in an organic solvent, then drop-wisely adding pure liquid dimethylamine, continuously reacting and processing.    USE - The method is useful for preparing 2,4-D-dimethylamine salt (claimed).    ADVANTAGE - The granule is simple and economical to prepare. The method does not utilize dangerous chemicals, dust and organic solvents, hence it is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing 2,4-D-dimethylamine salt water soluble granule, comprising adding auxiliary material into 2,4-D-dimethylamine salt, mixing uniformly, carrying out extrusion-granulation and drying.
NOVELTY - Marigold is dried, crushed, extracted using aqueous ethanol two times or more, and extract is concentrated. The extract is supplied into supercritical extraction device, and extracted by providing supercritical carbon dioxide as solvent and anhydrous ethanol as entrainer, to obtain extract. The extract is dissolved in ethanol, sedimented, supernatant is separated using macroporous resin, washed with water until, eluted using 45-90% ethanol as eluent, eluate is concentrated, concentrated solution is cooled, filtered and vacuum dried, to obtain macroporous resin and extract.    USE - Extraction of zeaxanthin from marigold (claimed).    ADVANTAGE - The method enables environmentally-friendly extraction of zeaxanthin from marigold, and provides nontoxic and harmless zeaxanthin having high quality with high recovery rate avoiding toxic reagents and reducing solvent residue.    DETAILED DESCRIPTION - Marigold is dried, crushed, extracted using 70-95 vol.% aqueous ethanol by heating at reflux under reduced pressure two times or more at 60-85 degrees C for 90 minutes or more under vacuum degree of 0.7-0.1 MPa, and extract is concentrated at 80 degrees C or less under vacuum degree of 0.7-0.1 MPa, such that the solid-liquid volume ratio of concentrate is 1:10-15. The extract is supplied into supercritical extraction device, and extracted by providing supercritical carbon dioxide as solvent at flow rate of 10-20 L/hour and anhydrous ethanol as entrainer at 35-50 degrees C and 45-60 MPa for 85-100 minutes, to obtain extract. The extract is dissolved in ethanol, sedimented, supernatant is separated using macroporous resin, washed with water until to neutral, eluted using 45-90% ethanol as eluent, eluate is concentrated to baume degree of 12-15, concentrated solution is cooled, filtered and vacuum dried, to obtain macroporous resin and extract in volume ratio of 1:8-13. The amount of aqueous ethanol is 9-12 times the amount of raw material.
NOVELTY - Calcining method comprises providing raw materials comprising whitlockite, iron phosphate, aluminum phosphate and/or fluorapatite, providing an alkali metal-sulfur compound as an additive, and calcining a mixture of the raw materials with the additive under reducing conditions at 800-1100 degrees C, preferably 850-1000 degrees C, to obtain a product comprising citrate-soluble phosphate compound.    USE - The calcining method is useful for obtaining a product comprising citrate-soluble phosphate compound to recover phosphate and to produce phosphate-containing fertilizer using sewage sludge (all claimed).    ADVANTAGE - The method is simple, economical and environmentally friendly. The phosphate-containing fertilizer improves soil fertility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) phosphorus-containing fertilizer obtained by above method using sewage sludge ash;    (2) citrate-soluble phosphate compound recovered from phosphorus containing raw material containing phosphorus phase including whitlockite, iron phosphate, aluminum phosphate and/or fluorapatite, where the method comprises determining molar ratio of sodium/silicon and a molar ratio of sodium/phosphorus in the raw material, determining an amount of sodium-sulfur compound, based on the molar ratios, and calcining the raw material and determined amount of sodium-sulfur compound under reducing conditions;    (3) use of the citrate-soluble phosphate compound for producing phosphorus-containing fertilizer; and    (4) obtaining phosphorus-containing fertilizer, comprising providing the above citrate-soluble phosphate compound or product comprising citrate-soluble phosphate compound, crushing the citrate-soluble phosphate compound, adding nitrogen-containing portion containing ammonium anion and/or urea to citrate-soluble phosphate compound, and granulating the mixture to specific particle size.
NOVELTY - Method for planting corn, involves selecting farmland and soil, providing ditch, applying pesticide to the soil of farmland, performing weeding process and tillage, applying suitable amount of fertilizer to the soil, supplying nutrients required for growth of corn to the farmland, applying pesticide to the farmland for controlling pests, performing weeding process, sowing corn seeds in the farmland, applying fertilizer to the corn, and supplying nutrients required for growth of corn. The fertilizer contains water, straw, compound fertilizer and manganese sulfate.    USE - The method is useful for planting corn (claimed).    ADVANTAGE - The method improves yield of corn, is environmentally-friendly, controls diseases and insect pests of corn, and produces corn which is highly nutritious and has high quality.    DETAILED DESCRIPTION - Method for planting corn, involves selecting farmland and soil, providing ditch, applying pesticide to the soil of farmland, performing weeding process and tillage, applying suitable amount of fertilizer to the soil, supplying nutrients required for growth of corn to the farmland, applying pesticide to the farmland for controlling pests, performing weeding process, sowing corn seeds in the farmland, applying fertilizer to the corn, and supplying nutrients required for growth of corn. The fertilizer comprises 60 wt.% water, 45-55 wt.% straw, 40-50 wt.% compound fertilizer, 1-2 wt.% urea, 1-2 wt.% zinc sulfate, 0.5-1 wt.% borax and 1-2 wt.% manganese sulfate. The fertilizer is prepared by crushing the straw, mixing crushed straw with the urea, zinc sulfate, borax and manganese sulfate, covering obtained mixture using plastic cloth, fermenting the mixture at 50 degrees C for 12-24 hours, turning the mixture during fermentation, increasing temperature of fermented product to 65 degrees C, adding urea and calcium phosphate to the mixture. The amount of fertilizer provided to corn during (i) seedling stage is 2%.
NOVELTY - Petroleum coke is removed from a coking operation, and a petroleum coke/water slurry is formed by adding water containing dissolved organic compounds to petroleum coke. A pH-lowering agent (A,B) is added to the slurry either during slurry formation or after slurry formation to form a treated petroleum coke/water slurry having reduced pH. The treated petroleum coke/water slurry having reduced pH is allowed to mix for a sufficient time in a carbon adsorption reactor to allow the petroleum coke to adsorb a portion of dissolved organic compounds from water.    USE - Treatment of water containing dissolved organic compounds e.g. oil sands process water from tailings settling basins of oil sands extraction operation, preferably surface mining operation (all claimed), bitumen extraction, and upgrading operation.    ADVANTAGE - The method uses petroleum coke, which is effective in treating oil sands process water produced during surface oil sands mining operations, and, particularly, when fresh product coke produced during fluid coking operations was used. The removal of dissolved organics present in process water is improved by addition of a pH-lowering agent to water/petroleum coke slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified schematic view explaining the water treatment process.    Slurry pump (71)    Slurry forming vessel (72)    Pipeline (74)    Coke cell (76)    Agent for lowering pH (A,B)
NOVELTY - Extraction of chemical compound from organism involves rupturing a cell wall of the organism using a solution comprising nanomaterials, and using an extraction solvent to extract the chemical compound.    USE - Extraction of chemical compound e.g. lipid, pigment, protein, carbohydrate and nucleic acid from organism e.g. microalgae and cyanobacteria (all claimed) used for biofuel production.    ADVANTAGE - The method enables economical, efficient and environmentally-friendly extraction of chemical compound from organism.
NOVELTY - The piston element (10) has heating apparatus (22) that is provided in outer periphery of reaction container (21), for pressurizing particle raw material (x) heated in container. Heat insulating material (122) is provided on opposite side to contact surface (121a) of thermally conductive material (121) which contacts the raw material, while providing thermally-conductive material in the side which contacts raw material in press portion (12) to pressurize the raw material. Corner-taking portion is provided in peripheral portion of contact surface in thermally-conductive material.    USE - Piston element used in molding apparatus (claimed) used for molding particle raw materials such as biomass ground materials.    ADVANTAGE - The center portion of the particle raw material is heated appropriately in reaction container, while suppressing the heat of the heated particle raw material escapes outside through piston element, when the particle raw material is pressurized in reaction container by piston element. Since the particle raw material is pressurized in reaction container by the press portion of the piston element, the heat from the heating apparatus provided in the outer periphery of reaction container is passed effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a molding apparatus is provided with clearance gap that is formed between inner surface of the reaction container and the press portion in piston element. The particle raw material in reaction container is pressurized by the pair of piston element from both sides.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the piston element.    Piston element (10)    Press portion (12)    Reaction container (21)    Heating apparatus (22)    Thermally conductive material (121)    Contact surface (121a)    Heat insulating material (122)
NOVELTY - A molding apparatus comprises heater (11) which makes reaction container (10) heat the molding of compression-molded particle raw material (xa), and cooling unit (12) which cools heated molding and has internal diameter larger than internal diameter of heater (D1).    USE - A molding apparatus (claimed).    ADVANTAGE - Inner surface of reaction container is not damaged and heated molding is smoothly guided to cooling unit. Production of vibration or noise is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional explanatory view of the molding apparatus.    Reaction container (10)    Heater (11)    Cooling unit (12)    Internal diameter of heater (D1)    Particle raw material (xa)
NOVELTY - The apparatus has a reaction chamber that is provided with an upstream end (7) and a downstream end (9). An inlet for organic feed material and the separate outlets for gas product are provided. The dried and pyrolysed solid carbon-containing product is produced from the organic feed material in the chamber. An assembly is provided for moving the organic material through the reaction chamber from the upstream end towards the downstream end to a flow of gas produced in the chamber.    USE - Apparatus for pyrolysing or processing solid organic feed material such as biomass, peat, coal, oil shale/sand, plastic waste material.    ADVANTAGE - The escape of gas from the reaction chamber via the extruder is prevented. The risk of gas leakage from the apparatus is minimized. The excessive build-up of accretions in the chamber is prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for pyrolysing or processing solid organic feed material;    (2) a method for starting apparatus; and    (3) a method for generating electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the apparatus for pyrolysing or processing solid organic feed material.    Converter (3)    Upstream end (7)    Downstream end (9)
NOVELTY - The generator has a switching mechanism (4) located in a fire grate (1). A furnace body (2) is formed with a fuel gas outlet (6) and an air entrance (7), where the fuel gas outlet is located in the fire grate and fixed with a lower part of the air entrance. A waste gas valve (9) and an electromagnetic heating plate (10) are fixed together. A top part (3) of the furnace body is formed with a material feeding entrance (12). An upper valve (13) and a lower valve (14) are fixedly connected together. The switching mechanism comprises a fixed clapboard (15).    USE - Adjustable plant combustible fuel gas generator for use in a rural area and a municipal area.    ADVANTAGE - The generator adopts an integral structure by combining a downdraft furnace body for pyrolytic gasification of materials and updraft furnace bodies for the dry distillation of materials so as to increase gas production rate, reduce production of tar oil, and ensure mutual switching between the dry distillation and pyrolysis of materials by the switching mechanism for realizing multiple functions. The generator is simple to use, and has low running cost, high safety, high reliability, better heating effect, better temperature control effect, and avoids tar outlet pipe blocking phenomenon.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an adjustable plant combustible fuel gas generator.    Fire grate (1)    Furnace body (2)    Top part (3)    Switching mechanism (4)    Fuel gas outlet (6)    Air entrance (7)    Waste gas valve (9)    Electromagnetic heating plate (10)    Material feeding entrance (12)    Upper valve (13)    Lower valve (14)    Fixed clapboard (15)
NOVELTY - A composition comprises a crosslinked polymer (I).    USE - Composition is used for forming gas-separation membrane used in separation of gas mixture (all claimed). Uses include but are not limited to purification of water, flammable fluid protection, flammable chemical storage and transportation, onboard oil tanker, inert fuel tank of aircraft, storage of food and flowers, tire inflation, wave soldering, laser cutting, annealing, etc.    ADVANTAGE - The composition provides gas-separation membrane with excellent separation performance and durability, and is economical.    DETAILED DESCRIPTION - A composition comprises a crosslinked polymer of formula: -(A-O-B'-O)n- (I).    A=-Ar1-Q-Ar2-, -Ar1-, or -Ar1-Ar2-;    B'=-Ar'1-Q'-Ar'2-, -Ar'1-, or -Ar'1-Ar'2'-;    Ar1,Ar2,Ar'1,Ar'2=bivalent 5-24C arylenyl or bivalent 5-24C heterocyclyl (both optionally substituted by R1 comprising a benzylic hydrogen);    R1=H, halo, -CN, -SO3H or its salt, -CO2H or its salt, 1-10C alkoxy, 1-10C haloalkyl, 1-10C haloalkoxy, or 1-10C alkyl, phenyl, or cyclohexyl (all optionally substituted), in which 2 or more R1 forms ring by joining together or covalently bonds to Y';    Y'=-O-, -S-, -C(=O), -CH(OH)-, -S(=O)-, -Si(CH3)2-, -(CH2)p-, -(CF2)q-, -C(CH3)2-, -C(CF3)2-, or -C(=O)NR1-;    Q,Q'=-O-, -S-, -C(=O), -CH(OH)-, -S(=O)2-, -Si(CH3)2-, -(CH2)p-, -(CF2)q-, -C(CH3)2-, -C(CF3)2-, -C(R1)(R1)-, C(=O)NH-, -P(=O)C6H5-, -C(CH3)(CF3)-, -C(=O)C6H4C(=O)-, -C(R1)(R1)-C6H4-C(R1)(R1)-, -phenyl-(1-6C)alkyl, -phenyl-(1-6C)haloalkyl, or phenyl, cycloalkyl, or heterocyclyl (all optionally substituted), in which R1 forms optionally substituted ring by joining together;and    p,q=1-10.    The at least one occurrence of Q or Q' contains an ultraviolet activator. INDEPENDENT CLAIMS are included for the following:    (1) gas-separation membrane;    (2) gas separation method; and    (3) formation of gas-separation membrane.
NOVELTY - Method for co-production of ethanol and biodiesel fuel using corn as feedstock involves (a) operating ethanol plant to produce ethanol-containing beer, (b) operating biodiesel plant comprising reactor assembly operably coupled with the ethanol plant apparatus to receive at least portion of corn oil product from the ethanol plant, and (c) transferring at least one stream of by-products to the ethanol plant downstream of fermentation apparatus and mixing with ethanol-containing beer before distillation within distillation apparatus.    USE - The method is useful for co-producing ethanol and biodiesel fuel using corn as feedstock (claimed).    DETAILED DESCRIPTION - Method for co-production of ethanol and biodiesel fuel using corn as feedstock involves (a) operating ethanol plant comprising fermentation apparatus to produce ethanol-containing beer and distillation apparatus to produce ethanol and corn oil product from the ethanol-containing beer, (b) operating biodiesel plant comprising reactor assembly operably coupled with the ethanol plant apparatus to receive at least portion of corn oil product from the ethanol plant, and reacting the corn oil with alcohol to produce biodiesel fuel and one or more by-products chosen from methanol, ethanol, glycerol, and their combinations, and (c) transferring at least one stream of by-products comprising 10 wt.% ester or less to the ethanol plant downstream of fermentation apparatus and mixing the by-products with ethanol-containing beer before distillation within distillation apparatus or mixing with stillage stream of distillation apparatus undergoing concentration within the ethanol plant.
NOVELTY - Preparation of carbon monoxide (CO) and hydrogen (H2) from biomass or component of biomass or from carbohydrate involves performing step (a) of contacting biomass, biomass component, or carbohydrate with polyoxometalate catalyst or its solvate in the presence of concentrated acid, under conditions sufficient to produce CO and optionally carbon dioxide (CO2), and performing step (b) of electrochemically producing H2 in which steps (a) and (b) are performed simultaneously or sequentially.    USE - Preparation of carbon monoxide and hydrogen from biomass or component of biomass or from carbohydrate (claimed).    ADVANTAGE - Reaction may be repeated for greater than or equal to 1 additional cycle, without the need to recycle or recover solvent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing formic acid from carbohydrate which involves contacting carbohydrate with polyoxometalate catalyst or its solvate in solvent selected from alcohol or mixture of alcohol and water under conditions sufficient to produce formic acid.
NOVELTY - Production of purified gas stream involves removing contaminants from feed gas stream, separating sour gas stream comprising hydrogen sulfide and mercaptans, converting hydrogen sulfide into elemental sulfur in Claus unit, converting sulfur dioxide in off-gas stream to obtain other off-gas stream comprising hydrogen sulfide, and converting mercaptans. Contact of residual gas stream comprising mercaptans with hydrogenation catalyst comprising nickel and molybdenum or nickel and tungsten supported on carrier is carried out in presence of hydrogen at 260-350 degrees C.    USE - Production of purified gas stream used as sweet gas.    ADVANTAGE - The method enables rapid production of purified gas stream containing less amount of hydrogen sulfide, with high yield.    DETAILED DESCRIPTION - Production of purified gas stream involves removing contaminants from feed gas stream to obtain the purified gas stream and sour gas stream comprising hydrogen sulfide and mercaptans, separating sour gas stream comprising hydrogen sulfide and mercaptans into gas stream enriched in hydrogen sulfide and residual gas stream comprising mercaptans, converting hydrogen sulfide in the gas stream enriched in hydrogen sulfide to elemental sulfur in Claus unit to obtain off-gas stream comprising sulfur dioxide, converting sulfur dioxide in off-gas stream comprising sulfur dioxide to hydrogen sulfide in Claus off-gas treating reactor to obtain other off-gas stream comprising hydrogen sulfide, and converting mercaptans from residual gas stream comprising mercaptans to hydrogen sulfide in mercaptans conversion reactor to obtain residual gas stream comprising hydrogen sulfide. Contact of residual gas stream comprising mercaptans with hydrogenation catalyst comprising nickel and molybdenum or nickel and tungsten supported on carrier is carried out in presence of hydrogen at 260-350 degrees C.
NOVELTY - Microbial fertilizer comprises nitrogen-fixing bacteria preserved in China center for type culture collection under accession no. (CCTCC M95040), Bacillus subtilis preserved in agricultural culture collection of China under accession no. (ACCC 11060), and potassium bacteria preserved in agricultural culture collection of China under accession no. (ACCC 10013).    USE - Microbial fertilizer used for planting lettuce (claimed).    ADVANTAGE - The microbial fertilizer increases yield and reduces nitrate concentration in lettuce.
NOVELTY - Manure comprises 5-15 pts. wt. dairy manure, 5-15 pts. wt. chicken manure, 5-15 pts. wt. pig manure, 10-20 pts. wt. tea oil cake, 10-20 pts. wt. tung oil cake, 5-15 pts. wt. strawberry peel, 15-40 pts. wt. tea peel, 3-10 pts. wt. tung peel, 3-10 pts. wt. phosphorus powder and 50-80 pts. wt. liquid methane.    USE - Manure.    ADVANTAGE - The manure has increased efficiency and kills underground insect and pathogens.
NOVELTY - A solid fermentation drying machine composed by an air heater, a fan, a refrigerant heat exchanger, humidifier, tail air drying heat exchanger, a feeding conveyor, a feeding chute, a fermentation groove, centre upright post, a rotating beam rack, a flat machine, spiral machine, a sieve plate, a discharging conveyer one. By feeding conveyor through material feeding chute is sent to fermentation groove carrying out fermentation, fermentation process and according to process requirement, through adjusting air quantity and adding water (spray) quantity adjustment.. a material humidity to ensure the normal proceed after finish, a air heater, a fan to carry out drying material. This utility new type, finish the fermentation, drying is finished in a same device, structure is simple, operation is convenient, production efficiency is high, the solid biological fermentation, which not only increase the protein content of product, increase the additional value of product, increase the economic benefit, but also avoids the waste residue to produce pollute environment, to a has protection effect.
NOVELTY - The system has a gasifier that is arranged with two outer circular chambers (4) and two inner circular chambers (3). A set of ports is arranged for loading and unloading of the system, where the ports are arranged in a horizontal shape. A pipe is arranged for removal of gases from an upper part of the gasifier. The outer circular chambers are provided with a thermal insulation. A set of circular heating tubes is arranged in the system. A set of heat exchangers (20) is arranged in a heating or cooling system.    USE - System for treating solid cellulose materials such as coal and wood, in industries and communities.    ADVANTAGE - The gasifier is arranged with two outer circular chambers and two inner circular chambers, thus allowing treating of solid cellulose materials with maximum yield, and enabling better utilization of the cellulose materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for treating solid cellulose material.'(Drawing includes non-English language text)'    Inner circular chambers (3)    Outer circular chambers (4)    Funnel shaped bottom (10)    Residues (11)    Heat exchangers (20)
NOVELTY - The process involves measuring the temperature of a methanol water fuel (11) earlier to the introduction of fuel into a combustion chamber of a compression ignition (CI) engine (3). The temperature of the fuel is controlled to control the viscosity of the fuel earlier to the introduction into the combustion chamber of the CI engine. An intake air (13) which is introduced into the combustion chamber of the engine is fumigated with a fumigant (14) having dimethyl ether as the ignition enhancer.    USE - Process for operating compression ignition engine by temperature adjustment to modify viscosity of fuel (claimed).    ADVANTAGE - The usage of new fuel compositions having physical properties that differ from usual fuels are enabled with an improved emissions profile without a major adverse impact on fuel efficiency and/or engine performance. The cooling of the fuel earlier to introduction of the fuel into the combustion chamber is made possible to obtain a sufficient increase in the viscosity of the fuel to enable operation of the methanol-water fuel in the CI engine in place of a diesel fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for operating CI engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system with a fuel storage unit, cooling unit and CI engine.    Cooling system (2)    Compression ignition engine (3)    Methanol water fuel (11)    Intake air (13)    Fumigant (14)
NOVELTY - The reactor has a chamber (1) for heating a gasification medium and connected with a top portion of a reservoir (2). An ash chamber (5) is placed with the chamber. Two truncated cones are connected with each other for forming a structural constriction part (9), and a bottom portion of the chamber is positioned at a rotating grate (15). A flame tube (8) is mounted on a helical tube system (10) and horizontally placed with respect to an encircling chamber (12). An inlet tube (13) is provided with a gasifying agent.    USE - Reactor for gasifying biomass and waste with high carbon content for generating renewable energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reactor.    Chamber (1)    Reservoir (2)    Ash chamber (5)    Flame tube (8)    Structural constriction part (9)    Helical tube system (10)    Encircling chamber (12)    Inlet tube (13)    Rotating grate (15)
NOVELTY - Producing oil involves accumulating oil in a structure by culturing oil-producing microalgae which is attached on to a structure formed of stimuli-responsive polymer, processing the structure in which oil is accumulated, and decreasing the volume of the structure in order to release oil from the structure by contracting the structure, where the microalgae is non-cytotoxic.    USE - The method is useful for producing oil, preferably biofuel (all claimed).    ADVANTAGE - The method is cost-effective and easy, conserves energy, and improves recovery efficiency of oil.
NOVELTY - A folium llicis latifoliae fertilizer comprises 40-50 pts. wt. inorganic fertilizer, 20-30 pts. wt. organic matter, 0.1-0.5 pts. wt. trace elements, 0.05-0.1 pt.wt. fertilizer activator, 0.1-0.5 pts. wt. water retention agent, 0.1-0.5 pts. wt. soil conditioner, and 0.05-0.1 pt.wt. insect repellent.    USE - Folium llicis latifoliae fertilizer.    ADVANTAGE - The fertilizer provides nutrition supplement needed for growth, can increase organic substance content in soil, improves soil environment, increases folium llicis latifoliae yield to more than 10%, and it has good pest repelling effect.    DETAILED DESCRIPTION - A folium llicis latifoliae fertilizer comprises 40-50 pts. wt. inorganic fertilizer, 20-30 pts. wt. organic matter, 0.1-0.5 pts. wt. trace elements, 0.05-0.1 pt.wt. fertilizer activator, 0.1-0.5 pts. wt. water retention agent, 0.1-0.5 pts. wt. soil conditioner, and 0.05-0.1 pt.wt. insect repellent. The inorganic fertilizer comprises nitrogen, phosphorus and potassium at mass ratio of potassium of 15-20:5-10:5- 10. The organic matter comprises municipal sewage treatment plant sludge, pulp and paper sludge, pharmaceutical factory Chinese medicine residue, pond sludge or pig manure heap fermentation product. An INDEPENDENT CLAIM is included for preparation of fertilizer comprising mixing insect repellent, trace elements, fertilizer activator, water retention agent, soil conditioner and organic matter, adding inorganic fertilizer, mixing, grinding through automatic feeding system, blending, granulating through drum granulator, sieving, automatic packaging, and inspecting.
NOVELTY - Method for cultivating golden needle mushroom, involves preparing culture medium using crop straw, sawdust, soybean powder, lime, urea, ammonium sulfate, potassium dihydrogen phosphate, calcium sulfate, ferric sulfate and magnesium sulfate, packing the culture medium in polyethylene bags, sterilizing the culture medium, cooling sterilized medium, inoculating the golden needle mushroom into the culture medium, cultivating and harvesting the golden needle mushroom.    USE - The method is useful for cultivating golden needle mushroom (claimed).    ADVANTAGE - The method cultivates golden mushroom which is rich in nutritional components, causes no pollution, and avoids usage of chemical fertilizer, pesticide and disinfectant. The mushroom causes no pollution to environment, and has improved fruiting rate.    DETAILED DESCRIPTION - Method for cultivating golden needle mushroom, involves (a) preparing culture medium by mixing 40-60% crop straw, 20-35% sawdust, 10-15% soybean powder, 1% lime, 3% urea, 2-3% ammonium sulfate, 1-2% potassium dihydrogen phosphate, 1-2% calcium sulfate, 1-2% ferric sulfate and 1-2% magnesium sulfate, uniformly stirring obtaining mixture, and adding water to the mixture, where moisture content of the mixture reaches 60-65%, (b) packing the culture medium in polyethylene bags, and binding the bags, (c) sterilizing the culture medium at 100 degrees C and normal pressure for 10-12 hours, (d) cooling sterilized medium to 20-30 degrees C, (e) inoculating the golden needle mushroom into the culture medium, (f) maintaining cultivation temperature at 22-26 degrees C, (g) placing the golden needle mushroom in greenhouse, and controlling temperature of the greenhouse at 8-14 degrees C, where relative humidity is maintained at 80-90%, and (h) harvesting the golden needle mushroom.
NOVELTY - Vanadium catalyst comprises activated carbon as a carrier, metal vanadium as active ingredient and carbonitride material as coating. The carbonitride material is formed by calcination of dicyandiamide raw materials under an inert atmosphere. The mass ratio of vanadium metal, raw material and activated carbon carrier is 1:(2-7):(15-60).    USE - The vanadium catalyst is useful for catalytic synthesis of 2,3,5-trimethyl benzoquinone (claimed).    ADVANTAGE - The catalyst: has good activity and selectivity; and is easy to recycle and reuse. The method: is simple; utilizes economical raw materials; and is suitable for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the vanadium catalyst, comprising dissolving vanadium metal compound in a solvent, adding the activated carbon, stirring, adding the raw material in an oil bath pot at 40-60 degrees C, dissolving after stirring continuously, subjecting to rotary evaporation in a rotary evaporator, drying the solvent in a vacuum drying chamber to obtain dry pre-catalyst material, sintering the pre-catalyst material under inert gas atmosphere to obtain vanadium catalyst material coated with carbonitride; and    (2) catalytic synthesis of 2,3,5-trimethyl benzoquinone using the vanadium catalyst, comprising adding 2,3,6-trimethylphenol, hydrogen peroxide and catalyst in organic solution, and the reacting at 30-60 degrees C for 4-6 hours to obtain the reaction product.
NOVELTY - Preparing organic fertilizer involves crushing domestic garbage and organic garbage to obtain mixture. Impurities and slag are removed from mixture using sand sediments. The mixture is crushed, mixed and then heated to obtain another mixture. The obtained mixture is put into anaerobic digestion reactor and then fermentation is performed to obtain fermentation material and biogas. The biogas is desulfurized and then stored in storage tank. The fermentation material is granulated to obtain the product.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method requires small floor area, and disposes organic waste rapidly and does not cause pollution.
NOVELTY - Composting garden plant waste involves pre-processing garden plant waste by collecting, sorting and trimming process. The pre-processed garden plant waste is mixed with non-hazardous waste. The garden plant waste is chipped. The chipped garden plant waste is fermented with conditioners and effective micro-organism at 55-65 degrees C for 10 days. The conditioning agent is compost or carbide material. The fermented material is ground to obtain compost powder that is further fermented with additives at less than 40 degrees C for more than 15 days. The compost material is urea, superphosphate or their mixture.    USE - Method for composting garden plant waste (claimed).    ADVANTAGE - The method enables to compost garden plant waste in simple, rapid and cost-effective manner with industrial applicability.
NOVELTY - Biofertilizer comprises 80-90 pts. wt. crop straw, 0.01-0.02 pts. wt. Aschersonia powder, 9-12 pts. wt. rapeseed cake, 90-120 pts. wt. chicken manure, 30-40 pts. wt. rice bran, 50-60 pts. wt. pig manure, 8-10 pts. wt. potassium dihydrogen phosphate, 6-9 pts. wt. sodium trimetaphosphate, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 0.003-0.008 pts. wt. caterpillar fungus powder, 3-9 pts. wt. litseae root, 9-12 pts. wt. tuber of dwarf lilyturf and 1-2 pts. wt. Stemona japonica.    USE - The biofertilizer is useful for preventing crop diseases (claimed) e.g. blight disease, damping-off disease, rust disease, Fusarium wilt, Rhizoctonia solani infection, verticillium wilt and root rot, preventing and controlling underground insect pests, and repelling and reducing reproduction rate of underground insect pests.
NOVELTY - Microorganism containing organic fertilizer comprises 100-120 pts. wt. chicken manure, 25-30 pts. wt. clove wooden meal, 15-20 pts. wt. jasmine wooden meal, 0.01-0.02 pts. wt. nitrogen-fixing bacteria powder, 0.01-0.02 pts. wt. Bacillus cereus powder, 0.01-0.02 pts. wt. B.thuringiensis powder, 25-30 pts. wt. rice straw, 1-2 pts. wt. humic acid, 55-60 pts. wt. peat, 15-35 pts. wt. soybean straw and 20-30 pts. wt. potato straw.    USE - The organic fertilizer is useful for preventing crop diseases e.g. blight disease, damping-off disease, rust disease, Fusarium wilt, Rhizoctonia solani infection, Verticillium wilt and root rot, preventing and controlling underground insect pests, and repelling and reducing reproduction rate of underground insect pests.
NOVELTY - Compound fertilizer comprises 18-25 pts. wt. diammonium hydrogen phosphate, 23-36 pts. wt. monocalcium phosphate, 1-6 pts. wt. stove subsoil, 9-14 pts. wt. honeysuckle stem, 14-21 pts. wt. Acacia tree sawdust, 15-20 pts. wt. grass charcoal, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 50-80 pts. wt. rice straw, 40-45 pts. wt. mud charcoal, 35-45 pts. wt. chicken manure, 55-60 pts. wt. potato straw, 0.1-0.3 pts. wt. lactic acid bacteria powder, 0.1-0.1-2 pts. wt. ocean Spirillum powder and 0.01-0.02 pts. wt. fermenting micro-organism.    USE - Compound fertilizer used for improving soil physical properties (claimed).    ADVANTAGE - The compound fertilizer ensures good water absorption and improves fertility of soil.
NOVELTY - A vehicle urea is produced by pumping liquid ammonia as raw material by high pressure, preheating after reaction of carbon dioxide in urea synthesis tower, stripping product flow falling film, heating after large ammonia decomposition by section evaporation heater, vacuum separator section, section evaporation heater and section vacuum separator, melting 99.7% urine in urea, sending melted urea to granulating tower and sending to base or package by scraping machine and each level material belt.    USE - Production of vehicle urea (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the section vacuum separator.    Section vacuum separator (1)    Section (2)    Filter screen (3)    Pipe (4)
NOVELTY - Synthesizing histamine dihydrochloride comprises carrying out heating decarboxylation of histamine with L-histidine, p-methyl acetophenone, 4-methyl cyclohexanol as solvent, and cuprous catalyst, where cuprous bromide is used as catalyst; reacting the solution with the hydrogen chloride gas to obtain the histamine hydrochloride salt, and filtering the solid to obtain a cake; and dissolving the histamine monohydrochloride salt in methanol solution hydrogen chloride gas, refining with activated carbon, filtering, cooling, and crystallizing to obtain the histamine dihydrochloride.    USE - Method for synthesizing histamine dihydrochloride (claimed).    ADVANTAGE - The method reduces temperature of decarboxylation, reduces variety and content of unknown impurities, increases conversion rate of raw material, improves purity of the final product, reduces energy consumption, has easy industrialization, saves hydrogen chloride solution, and has simplified operation.
NOVELTY - The system has a mill (50) for receiving water-free waste of recyclable material for grinding particles with 3.0-5.0 centimetres. A drying unit (60) is utilized for receiving waste, where hot air is fed to a hot air biomass combustion generator (61). A biomass gasifier is arranged in a fixed or fluidized bed (70) that receives particulate waste and dry with maximum humidity around 10%. The biomass gasifier is utilized for generating fuel gas in a cooling and purification unit (80). An electrical energy generating unit (90) receives the fuel gas for generating electrical energy.    USE - System for treatment of urban rubbish and generating electrical power in industry.    ADVANTAGE - The system can avoid contaminant and high consumption of water, and generates gases with reduced cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for treatment of urban rubbish.'(Drawing includes non-English language text)'    Mill (50)    Drying unit (60)    Hot air biomass combustion generator (61)    Fixed or fluidized bed (70)    Cooling and purification unit (80)    Electrical energy generating unit (90)
NOVELTY - This utility new type belongs to automotive urea solution production device field, especially relates to a one automotive urea solution production for environment-friendly device, wherein comprising a water inlet pipe, three-way inflow valve, a PP cotton filter, a control valve and the second PP cotton filter, a water pump, a first active carbon filter, the first extrusion active carbon filter, third PP cotton filter, ultra-filtration film filter, nanofiltration membrane filter, a reverse osmosis film filter, mixing tank, fourth PP cotton filter, a second active carbon filter, the second water pump, the second extrusion active carbon filter, fifth PP cotton filter, the second reverse osmosis film filter, the third reverse osmosis film filter, finished product tank, a waste water tank. This utility new type provide the one for a re-using waste water, saves water resource of automotive urea solution production for environment-friendly device.
NOVELTY - A tomato planting method includes wrapping seeds in gauze wrap, soaking in sodium phosphate solution, washing with water, soaking in warm water, taking out, and drying; spraying with aqueous urea, selecting tomato planting area, spreading with fertilizer, combining with soil, placing planting ditch, and planting seeds; adding livestock and poultry manure, ceramsite, slow-release granular fertilizer and soil conditioner; furrowing, watering, inserting bracket, and pruning leaves and branches; and controlling bacterial wilt, late blight and various diseases, and placing into sunny area.    USE - Method for planting tomato (claimed).    ADVANTAGE - The method is simple, easy to operate, scientific and reasonable, reduces inorganic fertilizer application amount, does not pollute the environment, and ensures quality of fruit.    DETAILED DESCRIPTION - A tomato planting method comprises:    (A) wrapping seeds in gauze wrap, soaking in 10 wt.% sodium phosphate solution for 15-25 minutes, washing with water, soaking in warm water at 28-32 degrees C for 2-3 hours, taking out, and drying;    (B) spraying with 0.1-0.2 wt.% aqueous urea;    (C) selecting tomato planting area, spreading with fertilizer, combining with soil, placing 1.3-1.7 m planting ditch having spacing of 40-50 cm, pruning, and planting 1500-2000 acres seeds; and adding 550-600 kg/acre livestock and poultry manure, 60-80 kg/acre ceramsite, 300-400 kg/acre slow-release granular fertilizer and 100-140 kg/acre soil conditioner;    (D) furrowing, watering, inserting bracket when tomatoes grow to 30-40 cm high, and pruning leaves and branches; and    (E) controlling bacterial wilt, late blight and various diseases, placing into sunny area, and avoiding rainy days.
NOVELTY - This utility new type relates to edible a medium device, specifically a a coffee grounds to a raw material of edible a medium device, comprising pressing plate, a gauze, yarn cloth two, support cover, fixing frame and without cover; the A to a coffee grounds is raw material of edible a culture medium c a rapid mounting and dismounting, convenient to carry after, and laying the two layer thin gauze, this not only can prevent to pollute medium, but also would not influence of environment, safe environment-friendly inner room, the temperature of edible medium need. culture medium at a different stage of carrying out statistical analysis, has the the circular temperature induction device does not need person to fix temperature testing device, the temperature sensor is inserted in inner medium is closer to a medium temperature, through position adjustment of temperature sensor, a measured inner medium and a different temperature and a different time period.
NOVELTY - 6-methyl-6H-benzo(4,5)thieno(2,3-b)indole and its derivative is new.    USE - 6-methyl-6H-benzo(4,5)thieno(2,3-b)indole and its derivative for functional material and pesticide.    ADVANTAGE - Product has stable structure and good chemical property, and synthesis process reduces environmental pollution and saves resource and energy.    DETAILED DESCRIPTION - 6-methyl-6H-benzo(4,5)thieno(2,3-b) indole of formula (I) and its derivative is new.    R1=1-8C alkyl, alkoxy, halo, nitrile, or carboxylic acid ester;    R2=1-8C alkyl or optionally substituted benzyl; and    R3=1-5C alkyl, optionally substituted 6-11C aryl, or carboxylic acid ester.    An INDEPENDENT CLAIM is included for synthesis of 6-methyl-6H-benzo(4,5)thieno(2,3-b) indole of formula (I) and its derivative.    DESCRIPTION OF DRAWING(S) - The drawing shows a reaction diagram of synthesis of 6-methyl-6H-benzo(4,5)thieno(2,3-b)indole and its derivative.
NOVELTY - A continuous roller-type biomass molding fuel is prepared by pretreating raw material, placing raw material powder, adhesive fiber, and quicklime in stirring container, adding deionized water, adjust stirring speed, uniformly stirring, adjusting slurry viscosity with deionized water and quicklime, transferring slurry to roller-type coating head of coating machine, coating soft fiber paper as substrate, continuously roller pressing biomass raw material based on required coating thickness on substrate to obtain biomass raw material layer, oven drying, and winding to roll coating end.    USE - Preparation of continuous roller-type biomass molding fuel (claimed).    ADVANTAGE - The preparation increases production efficiency, saves raw material cost and device investment cost, reduces manufacturing cost, and obtains product which is convenient to transport and store and has flexible rolling.    DETAILED DESCRIPTION - A continuous roller-type biomass molding fuel is prepared by removing impurity of agricultural waste, lignin, and/or oil crops waste biomass as raw material, smashing, sieving to 10-100 meshes to obtain raw material powder, placing 80-90 wt.% raw material powder, 6-10 wt.% adhesive fiber, and 2-5 wt.% quicklime in stirring container, adding deionized water, adjust stirring speed, uniformly stirring to obtain pressure roller slurry, adjusting slurry viscosity based on degree of viscous slurry material with deionized water and quicklime to obtain continuous roller slurry having 2000-10000 mPa.s viscosity, transferring slurry to roller-type coating head of coating machine, coating soft fiber paper as substrate, continuously roller pressing biomass raw material based on required coating thickness on substrate to obtain biomass raw material layer, oven drying, and winding to roll coating end.
NOVELTY - A continuous roller type biomass molding fuel is prepared by pretreating agricultural waste, lignin, and/or oil crops waste biomass to obtain raw material powder, placing raw material powder, adhesive fiber, and quicklime in stirring container, adding deionized water, uniformly stirring to obtain roller pressure slurry, adjusting slurry viscosity with deionized water and quicklime, transferring slurry to roller coating machine to soft fiber paper as substrate, continuously roller pressing biomass raw material to obtain biomass raw material layer, oven drying, and winding.    USE - Preparation of continuous roller type biomass molding fuel (claimed).    ADVANTAGE - The preparation is convenient, reduces difficulty, ensures compactness of biomass molding fuel, saves raw material and device investment cost, does not need larger device, and obtains product which has fine gradient.    DETAILED DESCRIPTION - A continuous roller type biomass molding fuel is prepared by removing impurity of agricultural waste, lignin, and/or oil crops waste biomass, smashing, sieving to 10-100 meshes number to obtain raw material powder, placing 80-90 wt.% raw material powder, 6-10 wt.% adhesive fiber, and 2-5 wt.% quicklime in stirring container, adding deionized water, uniformly stirring to obtain roller pressure slurry, adjusting slurry viscosity with deionized water and quicklime to obtain slurry for continuous roller having 2000-10000 mPa.s viscosity, transferring slurry to roller coating machine to soft fiber paper as substrate, continuously roller pressing biomass raw material based on required coating thickness to obtain biomass raw material layer, oven drying, and winding.
NOVELTY - Treating solid waste, domestic waste or garbage, industrial and hospital effluent and synthetic compound, comprises disaggregating the waste by mixing organic material in tanks; passing down to the waste tanks or reactors with dynamic or static flow to chemical hydrolysis, treating with calcium hydroxide and distilling.    USE - The method is useful for treating solid waste, domestic waste or garbage, industrial and hospital effluent and synthetic compound to obtain product, which is useful for the synthesis of organic solvents comprising hexanes, furans, alkanes, ethers or anhydrous alcohol, themoplastic plastics for making resins, paints, varnishes or porous or non porous membranes, synthetic compounds or petroleum products, propyl alcohol, butyl, amyl, aldehydes including furufural, and esters (all claimed).    ADVANTAGE - The process allows for decontamination, separation, cleaning, washing, composting, recycling, and direct or indirect reduction of solid waste and industrial wastes (claimed).
NOVELTY - Crop straw particulate fuel comprises crop straw and plant waste including corn stalk, rice straw, wheat straw, cotton stalk, peanut straw, sweet potato straw, different weeds, rice hull or/and leaves. The particulate fuel is prepared by naturally drying the raw materials (moisture content of less than or equal to 16%), crushing into particles of less than 8 mm, mixing with water (moisture content of 18-22%), steaming to soften, carrying out compression molding in a flat molding machine, cooling and packaging the pelletized fuel having a particle size of 6-9 mm, length of 20-30 mm and moisture content of less than or equal to 14%.    USE - Used as crop straw particulate fuel.
NOVELTY - Fertilizer composition comprises 20-30 pts. wt. nitrogen fertilizer, 5-7 pts. wt. phosphate fertilizer, 12-14 pts. wt. potassium fertilizer, 3-5 pts. wt. (0.1%) potassium dihydrogen phosphate, 30-40 pts. wt. pomegranate rind, 20-40 pts. wt. herba houttuyniae, 15-17 pts. wt. soybean curb residue, 40-60 pts. wt. wheat bran, 80-90 pts. wt. peat, 0.5-0.7 pts. wt. fungus powder, 30-50 pts. wt sawdust and 100-120 pts. wt. water.    USE - Fertilizer composition used for cultivating Chrysanthemum (claimed).    ADVANTAGE - The fertilizer composition is prepared in cost-effective manner, and has slow release property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a composition, which involves:    (A) mixing crushed raw materials with water, and then stirring them; and    (B) sealing the obtained material and fermenting for 4-6 days, and then granulating them to obtain the finished product.
NOVELTY - Fertilizer comprises 17-19 pts. wt. biogas manure, 13-15 pts. wt. sesame cake fertilizer, 12-14 pts. wt. Sesbania green manure, 7-9 pts. wt. canal mud, 8-12 pts. wt. mushroom residue, 11-13 pts. wt. copper monosulfide, 5-7 pts. wt. peanut, 6-8 pts. wt. ferrous sulfate, 1-3 pts. wt. ammonium molybdate, 2-4 pts. wt. Agrobacterium tumefaciens fertilizer, 3-5 pts. wt. calcium nitrate, 2-4 pts. wt. mixture of humic acid and selenium fertilizer, 1-3 pts. wt. Bacillus preparation and 50-60 pts. wt. water.    USE - Fertilizer used for Scindapsus aureus (claimed).    ADVANTAGE - The fertilizer provides nutrition to Scindapsus aureus and promotes its growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing components with water and stirring for 45 minutes to obtain a product; and    (B) fermenting the product in a sealed container for 3.5 hours and then drying to obtain final product.
NOVELTY - Recovery of methanol during preparation of cefprozi intermediate involves reacting 7-phenylacetamido-3-chloromethyl-3-cephem-4-p-methoxybenzyl carboxylate (I) with sodium iodide and triphenylphosphine, obtaining phosphonium salt intermediate, carrying out witing reaction of phosphonium salt and acetaldehyde, obtaining 7-phenylacetamido-3-(prop-1-en-yl)-4-cephalosporanic acid methoxybenzyl ester (II), distilling off methylene chloride, dripping water and methanol in the product, filtering, obtaining mother liquor comprising methanol and water, and recovering methanol by evaporating.    USE - Recovery of methanol during preparation of cefprozi intermediate (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly recovery of methanol during preparation of cefprozi intermediate with high yield and quality.    DETAILED DESCRIPTION - Recovery of methanol during preparation of cefprozi intermediate involves reacting 7-phenylacetamido-3-chloromethyl-3-cephem-4-p-methoxybenzyl carboxylate of formula (I) with sodium iodide and triphenylphosphine, obtaining phosphonium salt intermediate, carrying out witing reaction of phosphonium salt and acetaldehyde, obtaining 7-phenylacetamido-3-(prop-1-en-yl)-4-cephalosporanic acid methoxybenzyl ester of formula (II), distilling off methylene chloride under reduced pressure, dripping water and methanol in 7-phenylacetamido-3-(prop-1-en-yl)-4-cephalosporanic acid methoxybenzyl ester precipitate, filtering the resultant reaction solution by suction filtration, obtaining filter cake comprising 7-phenylacetamido-3-(prop-1-en-yl)-4-cephalosporanic acid methoxybenzyl ester and filtrate mother liquor comprising methanol and water, transferring the mother liquor to the evaporator, and recovering methanol, determining the moisture content of recovered methanol, and carrying out further processes.
NOVELTY - Method for farming carp, involves constructing pond, farming carp in the pond, UV sterilizing fresh chicken manure at high temperature for 1-2 hours, mixing sterilized chicken manure with corn flour, adding obtained mixture to fermentation tank, fermenting the mixture for 20-30 days, granulating fermented product to obtain granular feed, feeding the carp using the granular feed during 6 am at morning and 4 pm at evening, then feeding the carp using traditional Chinese medicine for every 3-5 days, and changing pond water once for every 7-10 days.    USE - The method is useful for farming carp (claimed).    ADVANTAGE - The method cost-effectively farms carp, prevents growth of bacteria in stomach and intestine of carp, improves gastrointestinal motility of carp, and enhances disease resistance of carp.
NOVELTY - Method for ecologically farming cattle, involves farming cattle in farmland, adding cow dung to methane fermentation tank for producing biogas, processing obtained fermentation residues to obtain basal fertilizer, then processing crop straw of farmland to obtain coarse feed for cattle, and processing residual straw to produce biogas.    USE - The method is useful for ecologically farming cattle (claimed).    ADVANTAGE - The method is cost-effective to perform, and environmentally-friendly.
NOVELTY - Method for producing curly and pearl particle like wool, involves obtaining moderate hair density sheepskin, shearing, brushing, scalding, inspection and weighing, adjusting water content in sheepskin, respectively adding sodium hydrate, sodium bicarbonate, sodium hydrate, and 10% argon/methane mixture, paddling, drying, stretching, brushing, scalding, shearing, adding dissolved solution on sheepskin and brushing, drying, and trimming wool.    USE - The method is useful for producing curly and pearl particle like wool (claimed), which is useful for preparing collar and other ornaments.    DETAILED DESCRIPTION - Method for producing curly and pearl particle like wool, involves (a) obtaining moderate hair density sheepskin, shearing, brushing using water, scalding, shearing, brushing using formic acid solution, scalding, shearing, inspection and weighing, where the final shearing length is 1.2-1.5 cm, (b) adjusting water content in sheepskin, adding 2 g/l 5-10 times of sodium hydrate, paddling at 45 degrees C for 60 minutes, where the liquid ratio is 1:30, adding 1-1.5 g/l 5?10 times of sodium bicarbonate, and paddling at 45 degrees C for 60 minutes, where the pH is maintained at 6-6.5, (c) adjusting water content in sheepskin, adding 0.6 g/l5-10 times of sodium hydrate, paddling at 40 degrees C for 60 minutes, where the liquid ratio is 1:30, and the pH is 8, adding 5 g/l 10% argon/methane mixture, and paddling at 40 degrees C for 120 minutes, (d) adjusting water content in sheepskin, adding water (35 degrees C), paddling at 35 degrees C for 20 minutes, (e) drying, stretching, brushing, scalding and shearing to a length of 1.2-1.5 cm, (f) dissolving 1 g/l sodium sulfide, and 2 ml/l WEIJIA (RTM: Fur protecting agent) M-60 in water (60-65 degrees C), adding 30-50 ml dissolved solution on sheepskin and brushing, (g) subjecting processed sheepskin to drum, and drying at 40-45 degrees C for 6-10 hours, and (h) trimming wool.
NOVELTY - Fertilizer comprises 35-64 pts. wt. inorganic fertilizer, 20-40 pts. wt. organic fertilizer, 6-16 pts. wt. humic acid, 4-16 pts. wt. filler and microorganism, where the viable count of microorganism is not less than 8x 109 colony-forming unit (CFU).    USE - The fertilizer is useful for controlling Fusarium wilt of banana (claimed).    ADVANTAGE - The fertilizer improves yield of banana and microbial environment of soil, and reduces incidence of disease rate of banana.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) uniformly mixing components of organic fertilizer, piling and fermenting obtained mixture at 50-60 degrees C for 20-24 hours, and turning the mixture for 2-3 times during fermentation, (b) adding the microorganism to fermented product, fermenting the mixture at less than 25 degrees C degrees centigrade, (c) mixing fermented product obtained in step (b) with the humic acid and filler, crushing, drying and granulating obtained mixture, and (d) mixing granules with the inorganic fertilizer to obtain product.
NOVELTY - Composting straw involves (a) digging a pit in a field near water bodies to stack straw and compost in the pit for long time period, (b) filling wheat or rice straw in the pit to the 50 cm thickness, covering the straw with soil and forming the heap having 1.5-2 m height and watering the formed heap, and (c) forming soil surface having 5 cm thickness, then forming heal of 20-50 cm height, covering heap with the plastic film, composting the straw staked for 45-70 days, under aerobic conditions, until the straw becomes dark brown, and naturally drying composted product.    USE - The method is useful for composting straw (claimed).    ADVANTAGE - The method enables to absorb water completely, and produce high quality straw compost.
NOVELTY - Fertilizer comprises 15-17 parts mass nitrogenous fertilizer, 8-12 parts mass phosphate fertilizer, 20-24 parts mass potash fertilizer, 50-70 parts mass dairy manure, 40-60 parts mass sheep manure, 20-40 parts mass apple powder, 10-20 parts mass coal gangue, 20-30 parts mass weathered coal, 8-10 parts mass humic acid, 5-7 parts mass K7 rare earth, 2-4 parts mass camphor and 120-140 parts mass water.    USE - The fertilizer is useful for Zelkova serrata (claimed).    ADVANTAGE - The fertilizer is prepared cost-effectively, environmentally-friendly, and easily degraded.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing the above-mentioned components except water using crusher, adding water to above-mentioned components, stirring obtained mixture, sealing the mixture, and granulating obtained product using granulator.
NOVELTY - Usage of sodium-based pyrolysis catalyst involves crushing rice husk, drying in an oven, filtering, adding sodium carbonate powder, mixing, pyrolyzing rice husk, and measuring experimental data based on analysis.    USE - Usage of sodium-based pyrolysis catalyst (claimed).
NOVELTY - Fertilizer comprises 15-20 pts. wt. organic fertilizer, 5-10 pts. wt. blood meal, 5-10 pts. wt. potassium sulfate, 2-5 pts. wt. phosphoric acid salt of an aromatic diamine, 1-2 pts. wt. ammonium sulfate, and 25-50 pts. wt. bentonite.    USE - As fertilizer for peach (claimed).    ADVANTAGE - The fertilizer is rich in nutrients, and environmentally-friendly, and increases yield of peach.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) mixing blood meal, organic fertilizer and bentonite in suitable proportion, (b) fermenting the mixture for 5-8 days, and (c) adding potassium sulfate, phosphoric acid salt of an aromatic diamine, and ammonium sulfate to the fermented mixture to obtain fertilizer base.
NOVELTY - Processing of starch wastewater discharged during biogas production involves supplying wastewater in conditioning tank, heating to reflux, supplying anaerobic tank, fermenting the isolated anaerobic biogas and sewage in the pool, storing the biogas in a temporary storage casks, desulfurizing in desulfurization apparatus, dehydrating the desulfurized gas, compressing the gas in compressor, storing the compressed gas in high-pressure gas package, and processing the wastewater in aerobic tank and settling tank in turns.    USE - Processing of starch wastewater discharged during biogas production (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables efficient and economical processing of starch wastewater discharged during biogas production with reduced energy consumption.
NOVELTY - Preparation of baked brick involves sorting household garbage, removing heavy metal garbage and plastic waste by dry separation, further removing noncombustible waste from the obtained dry waste, subjecting to thermal pyrolysis and gasification to obtain pyrolysis gas and pyrolysis residue, fermenting for 48-72 hours, adding 3-5 wt.% flocculant to the obtained fermentation product, stirring, carrying out sediment stratification, dehydrating, mixing obtained biogas with raw material and water, crushing, mixing, extruding, cutting and handling, aging, drying, and calcining.    USE - Preparation of baked brick used for energy-saving building material.    ADVANTAGE - The baked brick having high porosity and excellent thermal insulation property, is prepared.    DETAILED DESCRIPTION - Preparation of baked brick involves sorting household garbage, removing heavy metal garbage and plastic waste by dry separation, further removing noncombustible waste from the obtained dry waste, subjecting to thermal pyrolysis and gasification to obtain pyrolysis gas and pyrolysis residue, fermenting for 48-72 hours, adding 3-5 wt.% flocculant to the obtained fermentation product, stirring, carrying out sediment stratification, dehydrating, mixing obtained biogas with raw material having particle size of 5 mm or less, and water, crushing, mixing, extruding, cutting and handling, aging at 25-35 degrees C for 48-72 hours, drying at 100-150 degrees C for 1-20 hours, and calcining at 850-1100 degrees C for 16-32 hours. The water content of biogas is 50-60 %mass. The raw material is coal gangue, bentonite, shale, silica sand, fly ash and clay.
NOVELTY - Preparation of 4-hydroxyphthalic acid involves carrying out hydroxylation reaction of 4-bromophthalic anhydride and strong inorganic base in presence of catalyst and solvent, at 120-140 degrees C.    USE - Preparation of 4-hydroxyphthalic acid (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of 4-hydroxyphthalic acid having high purity, with high yield and low equipment requirements, under mild reaction conditions.
NOVELTY - The biodigestor has an inlet chamber (1) arranged inside the digester for biogas generation. A dome (3) stores the generated biogas. An outlet chamber (4) is provided with guides or rails (2) for positioning wagons. Semi-automatic shaking devices are provided with a crank, a worm shaft and a coupling element. A coordinate system transmits motion to the coupling element by positioning the rails of the digester. A rotation transmitting system is coupled with augers in the biodigestor.    USE - Biodigestor for production of biogas from agro waste, livestock and solid waste and storing biogas that is used in a vehicle.    ADVANTAGE - The biodigestor separates mixtures to increase biogas production, allow co-digestion of brine by-products from olives and empty each wagon in each cycle and prevent damage to a vehicle during biogas production process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a biodigestor.    Inlet chamber (1)    Rails (2)    Dome (3)    Outlet chamber (4)
NOVELTY - Method for multi-stage microbial treatment of livestock wastewater involves (a) processing the wastewater by using first anaerobic wastewater treatment system, (b) transferring the resulting water into a intermittent aerobic system, and processing the water, and (c) processing the obtained wastewater by using aerobic system.    USE - The method is useful for multi-stage microbial treatment of livestock wastewater (claimed).    ADVANTAGE - The method enables to achieve chemical oxygen demand (COD) and biochemical oxygen demand (BOD) by 10-40%, and remove ammonia, nitrogen and total nitrogen by 20-50%.    DETAILED DESCRIPTION - Method for multi-stage microbial treatment of livestock wastewater involves (a) processing the wastewater by using first anaerobic wastewater treatment system, (b) transferring the resulting water into a intermittent aerobic system, and processing the water, and (c) processing the obtained wastewater by using aerobic system, where (i) anaerobic wastewater treatment system involves using one or more Bacillus subtilis, B.licheniformis, B.pumilus, B.cereus, B.coagulans, and photosynthetic bacteria, (ii) intermittent aerobic system involves using one or more chosen from Bacillus pumilus, B.cereus, Pseudomonas stutzeri, P.putida, lactic acid bacteria, yeast, denitrifying bacteria and their combinations, and (iii) aerobic system involves using one or more chosen from B.subtilis, B.licheniformis, B.pumilus, B.cereus, B.coagulans, denitrifying bacteria, yeast and their combinations.
NOVELTY - Lipid microvesicle comprises phospholipid bilayer membrane, gas and carrier containing bleomycin and albumin nanoparticles, where the gas and carrier are wrapped inside the phospholipid bilayer membrane, and the albumin is bovine serum albumin.    USE - As lipid microvesicles containing bleomycin (claimed).    ADVANTAGE - The lipid microvesicles have high loading and encapsulation efficiency, improves blood concentration target site, and drug stability, extends duration of action of the drug at the target, reduces drug degradation, and side effects, and selectively promotes distribution of drug and thus helps delivery of drugs into diseased tissue. The method is easy, environmentally-friendly, and safe as it does not make use of toxic organic solvents.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the lipid microvesicles which involves (a) mixing bleomycin and ethanol, adding the mixture gradually to albumin solution, adding glutaraldehyde to the mixture, stirring the mixture for curing using a rotary evaporator to remove ethanol to obtain drug suspension containing albumin nanoparticles, and (b) mixing phospholipids, glycerin and phosphate buffer in a weight ratio of 55-60:5-8:100, adding suitable amount of suspension, heating the mixture, and charging with a gas.
NOVELTY - Preparation of nano cobalt chain comprises adding oleylamine solution and Cobalt acetate tetrahydrate into reaction kettle, magnetically stirring for 5 minutes, and uniformly dispersing; and sealing, introducing carbon monoxide (CO) gas, adjusting pressure to 0.02-0.1 MPa, and magnetically stirring at 100-200 degrees C for 5-12 hours; cross washing with cyclohexane and ethanol, magnetically separating, and drying at 60 degrees C.    USE - Method for preparing nano cobalt chain used for CO and hydrogen catalytic reaction (claimed).    ADVANTAGE - The nano cobalt chain has 250 nm uniform size and catalytic effect.
NOVELTY - A stable biodiesel additive comprises 5-10 pts. wt. N,N-dimethylformamide, 6-10 pts. wt. 8-nitroisoquinoline, 3-8 pts. wt. triethylorthoacetate, 4-6 pts. wt. cyclohexanone, 2-8 pts. wt. o-aminophenol, 3-5 pts. wt. cyclohexane, 6-11 pts. wt. polyalkylene glycol, 2-6 pts. wt. benzoyl peroxide, 3-7 pts. wt. spermine, 1-5 pts. wt. tert-butylhydroquinone, 5-10 pts. wt. cetyl dimethyl ammonium chloride, 1-5 pts. wt. diphenylamine, 3-6 pts. wt. benzenetriazole compounds, 1-4 pts. wt. petroleum sulfonate, and 1-3 pts. wt. modified additives.    USE - Stable biodiesel additive.    ADVANTAGE - The additive is low-cost.
NOVELTY - This utility new type claims a a scale and a high efficiency, stable running of biomass solid molding fuel molding machine. A a biomass solid molding fuel molding machine, wherein comprising pedestal, molding motor, a shaft joint, a feeder motor, feeder, material l, wherein discharging, molding room, a forced feeding device comprises horizontal feeding spiral, the arc forced feeding shaft, scraper, material l; the A a biomass solid molding fuel molding machine, provided with ring mould structure, and mounting 2 a pressure roller, a pressure roller set with rotating gap-adjusting wheel, pressure roller and a pressure roller fixing shaft a, a pressure roller shaft is eccentric of the rotating pressure roller shaft can change die roller, and rotating wheel for regulating gap mould roller; the forced under feeder provided with feeder motor, a forced feeding device of supply power, a pedestal provided with molding.; a ring mould provided with ring mould hole, the annular mould part provided with cutting knife.
NOVELTY - The utility model relates to a full fermentation anti-floating not bind shell biogas device, a fermentation tank and mounting a hood in fermentation tank feeding port, the upper part of the fermentation tank the lower part side face is set on slag has a drain hole, a skirt on a set has guide hole, and wherein the feeding fermentation tank is installed has a diameter slightly smaller than fermentation tank of feeding wherein a protecting anti-floating grate, a protecting floating grate at a feeding port on a lower, bottom and side wall of the fermentation tank provided with heating device and a vapour heating pipe. The utility model is new type provide a set with a simple structure, low cost of fermentation tank, a top cap skirt, a through open cap skirt take out protecting floating grate and adding raw material, a protecting floating grid using a liquid level higher than the protecting floating grate, the upper layer will not generate the layer, reducing the stirring device, saves cost, and gas total quantity exponentially increase, a solar energy roof and bottom heating device heating together, in a tank body capable of holding a high warm, all the year round can.
NOVELTY - The new type utility claims a heat preservation marsh gas pool using solar power supply, comprising biogas pool 1, the marsh gas pool 1. mounting has heating unit, a heating unit and a marsh gas 1 outside of 2. a storage battery, the storage battery 2 through biogas pool 1 outside the photovoltaic charging controller and solar energy power generation unit 3 a, the heating unit is a fan by a gas 1 outside 4, air heater 5, compressor 6 and a gas 1 in the heat exchange pipeline 7 through insulating tube 8 connected in turn. The utility model is new type of effect is good, structure is simple, suitable for wide range.
NOVELTY - The method involves providing a proton exchange membrane comprising an electrode (111) and another electrode (112). A reinforcement (131) is placed with an overlapping portion (133) that is vertically adjacent to a periphery of the membrane, and an extension portion (135). Another reinforcement (132) is arranged with an overlapping portion (134) and with an extension portion (136) extending laterally beyond the membrane. A laser beam (20) is applied to the vertically adjacent extension portion (135) so as to define an opening (40) through the extension portions to weld the extension portions.    USE - Method for manufacturing a membrane/electrode assembly that is utilized in a fuel cell. Can also be used for an electrolyser.    ADVANTAGE - The laser beam is applied to the vertically adjacent extension portion so as to define the opening through the extension portion to weld the extension portions, thus increasing power density of the electrode assembly, and manufacturing the electrode assembly with reduced steps.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a membrane/electrode assembly.    Laser beam (20)    Opening (40)    Electrodes (111, 112)    Reinforcements (131, 132)    Overlapping portions (133, 134)    Extension portions (135, 136)
NOVELTY - Production of hydrogen rich-gas comprises introducing water and argon gas into plasma generator by atomizing, subjecting pair of electrodes within the plasma generator to high voltage, generating electric arc breakdown, lower speed rotating, quenching, circulating, generating non-thermal plasma electric arc, carrying out plasma-induced chemical reaction, and water decomposing.    USE - Method for producing hydrogen rich-gas (claimed).    ADVANTAGE - The plasma generator has less equipment investment, greatly reduces power consumption and electrode loss, and is suitable for on-site hydrogen production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plasma generator comprising central electrode, PTFE layer, outer electrode, feeding port, cylinder outside wall, and air outlet.
NOVELTY - Treating sewage wastewater involves treating sewage wastewater in an effluent treatment chamber, where the processed fluid is passed through a downstream outlet pipe made of polyvinyl chloride (PVC). The downstream outlet pipe provided with a small hole, is further connected to a reflux tank, and then into a three-way solenoid valve. The generated fluid is passed through counter current exchangers, where the processed fluid passes through PVC baffles, and then to sewage treatment plant, which utilizes air and biological floc comprising microorganisms.    USE - Method for treating sewage wastewater in sealed reactor (claimed).    ADVANTAGE - The method enables to treat sewage wastewater in sealed reactor by effectively removing total phosphorus, total nitrogen, suspended solids contents, and other major pollutants in the sewage wastewater, thus lowering the chemical oxygen demand value of processed sewage wastewater.    DETAILED DESCRIPTION - Treating sewage wastewater involves treating sewage wastewater in an effluent treatment chamber, where the processed fluid is passed through a downstream outlet pipe made of polyvinyl chloride (PVC). The downstream outlet pipe provided with a small hole, is further connected to a reflux tank, and then into a three-way solenoid valve. The generated fluid is passed through counter current exchangers, where the processed fluid passes through PVC baffles, and then to sewage treatment plant, which utilizes air and biological floc comprising microorganisms. The sewage wastewater microbial treatment is performed for 4-6 hours, where after completion of the process, the obtained activated sludge from the processed sewage wastewater is passed to an aeration chamber, and then to a stable ecological system, which provides illumination for the photosynthesis of plants.
NOVELTY - Sealed sewage processing device comprises a seal housing (1), a sewage water inlet pipe (2), a processing plant (3), a microorganism treatment room (4), a microorganism water outlet room (5), a plant inlet room, a fan, an aeration pipe and a water outflow pipe. The seal housing top part is opened and closed with a window-shade. The window-shade is connected with the water inlet tube in one side of the seal housing. The seal housing internal plant is equipped with the microorganism treatment room. Water outflow pipe is polyvinyl chloride pipe.    USE - Sealed sewage processing device.    ADVANTAGE - The sealed sewage processing device is cost-effective, simple and energy saving, has strong processing capability by controlling the amount of chemical oxygen demand, total phosphorus, total nitrogen, suspended solids and other major pollutants.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sealed sewage processing device.    Seal housing (1)    Sewage water inlet pipe (2)    Processing plant (3)    Microorganism treatment room (4)    Microorganism water outlet room (5)
NOVELTY - Foliar fertilizer comprises vermicompost.    USE - Foliar fertilizer used for promoting growth, flowering and fruiting of crops.
NOVELTY - Destroying pathogenic bacteria involves adding buttermilk, molasses, sugar cane, sorghum, corn or other cereal into swine manure and mixing to obtain mixture. pH value of mixture is adjusted to 4.5 by lactic acid bacteria activity in 16 hours.    USE - Method for destroying pathogenic bacteria in swine solid waste (claimed).
NOVELTY - Reduction of carbon dioxide involves providing electrolyte containing dissolved carbon dioxide to sp2 bonded carbon electrode, and reducing dissolved carbon dioxide through electroreduction by powering the sp2 bonded carbon electrode.    USE - Reduction of carbon dioxide for producing carbon-based fuels and chemicals.    ADVANTAGE - The method enables efficient reduction of carbon dioxide with high catalytic conversion of carbon dioxide at low overpotential, providing carbon-based fuels with high energy density.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon dioxide reduction cell.
NOVELTY - Increasing elemental and nutritional content of plant seeds comprises cultivating plant seeds with Bacillus strain (MCC0008) as a biofertilizer which is capable of sequestering nitrate and phosphate from wastewater.    USE - Method for increasing elemental and nutritional content of plant seeds (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of enhancing germination of plant seeds by applying a Bacillus strain (MCC0008) with accumulated nitrate and phosphate as a fertilizer to soil during germination of the plant seeds.
NOVELTY - An oxygen reduction electrode catalyst carries boron nitride nanosheet which is provided on surface containing metal chosen from gold, nickel, palladium and platinum.    USE - Oxygen reduction electrode catalyst is used in electrode used for fuel cell and producing hydrogen (all claimed).    ADVANTAGE - The oxygen reduction electrode catalyst has improved catalytic activity, without using platinum, effectively suppresses generation of hydrogen peroxide by oxygen reductive reaction in electrode, improves oxygen reductive reaction catalyst activity by adjusting size of the boron nitride nanosheet, and provides electrode having high hydrogen generation reaction activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method to suppress generation of hydrogen peroxide by oxygen reductive reaction in electrode, and to improve oxygen reductive reaction catalyst activity by adjusting the size of the boron nitride nanosheet; and    (2) hydrogen-producing apparatus.
NOVELTY - The method involves using a heat pump (21) with magneto caloric effect to exchange heat between a cold source at subambiante temperature and a hot source with higher temperature. The heat pump is maintained in a cold apparatus by partially compensating thermal entries. A gas (13) is sent toward the heat pump using a dedicated controller, where a gas mixture (1) has principal components containing hydrogen, nitrogen, carbon monoxide, carbon dioxide and methane. A gas output condensed in an exchanger (17) is returned on an intermediate level of a column.    USE - Method for separating a gas mixture in a separation apparatus operating at subambient or cryogenic temperature.    ADVANTAGE - The method enables reducing starting time for separating the gas mixture in the separation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for separating a gas mixture in a separation apparatus operating at subambient or cryogenic temperature.    Gas mixture (1)    Gas (13)    Exchanger (17)    Heat pump (21)    Condenser head (35)
NOVELTY - Catalyst nanoparticles comprise a non-noble metal solid solution core, and a continuous and nonporous noble metal shell surrounding the non-noble metal solid solution core. The non-noble metal solid solution core comprises nitride of non-noble metal including nickel, cobalt, iron and/or copper.    USE - Catalyst nanoparticles are used for energy conversion device e.g. fuel cell (all claimed).    ADVANTAGE - The catalyst nanoparticles have excellent durability, high catalytic activity and reduced loading of precious metal, and are economically manufactured by simple process. The dissolution of core during potential cycle is suppressed. The lattice contraction leading to an up-shifted noble metal d-band center is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) formation of nitride-stabilized nanoparticles, which involves producing nanoparticles of metal (M1) by pulse potential deposition in a solution comprising a salt of metal (M1), or adding a chemical reducing agent to the solution comprising salt of metal (M1) or by heating a dry mixture of carbon and adsorbed metal (M1) ions in hydrogen, forming a shell layer of noble metal (M2) on an external surface of the nanoparticles, and annealing obtained core-shell nanoparticles under a nitrogen source to produce nitride of metal (M1); and    (2) energy conversion device.
NOVELTY - This utility new type claims a a three format integrated excrement pool, the utility model is new type of target is a supply a purification effect and a side effect of domestic sewage treatment tank, it comprises box body, end cover, clapboard for internal of box body by dividing into three of a, respectively a sewage area, purification area and purified water area, provided with more of the bottom of the box body in parallel and a supporting rod n a purification area, a supporting rod fixed at upper clapboard, and the tank body top is hung more pendulous rope of b at each branch pole is hung for strain to a component in a rope, the top of end cover is provided with a multi-hole and provided with observation and observation hole matching a cover integrated excrement pool in three format before after two end is provided with inflow hole and a water outlet hole, water hole and the water for the matching hole of the tank body and end cover, it comprises purification effect, green and environment-friendly, convenient to change strain equal.
NOVELTY - This utility new type relates to a a. cultivation sewage ecological purifier. The purifier comprises a floater, a cable, a sinker and multi-layer vertical array of biological carrier happen, the floater is equipped with a purifier top sinker set in the purifier, the multi-layer biological happen a top cable connected in series by a floater and a sinker between, the floater is provided with a self-controlling device, driving device, control device and mooring rope picking and picking device, a multi-layer biological happen carrier provided with the light frequency regulating device, temperature regulating system and light source, the bottom of the sinker set with touching induction device. This utility new type has simple structure, restrain alga growing, water quality purification, stable work, purification effect is fast, use life is long, the driving device a a b 360 degrees to a purifier, automatic control device comprises detection, identification, diagnosis, evaluation and response function, the effective work is stable.
NOVELTY - A a sewage processing device, a sewage collecting pipe, hoisting machine, filter cloth, acid-alkali storage tank, a pH regulating pool, the second acid-base regulating pool, Anaerobic decontamination tank, an aerobic decontamination tank, a blower module, concentrating tank, dry pulverizer and opposite permeability processing pool. A pH regulating pool and sewage collecting pipe far away from one terminal filter cloth is connected, acid-alkali storage tank and the acid regulating pool and the first connected a sewage collecting pipe is connected, the second acid-base regulating pool and a pH regulating pool connected, Anaerobic decontamination tank and the second acid-base regulating pool connected, aerobic decontamination tank respectively connected and Anaerobic decontamination tank and blast component, concentrating tank and aerobic decontamination tank connected, dry pulverizer and opposite permeability treatment pool and concentrating tank are connected. A a a a a a sewage sludge would not bring the heavy metal, is to obtain a sediment be used as agrochemical mud, reduces the quadratic pollute of sludge, which is good for a use of environmental protection and resource.
NOVELTY - This utility model claims a DNA purification device, comprising external pipe below the circle lengthways with a DNA purification tube and bug internal provided with a circle of transverse of a pipe bug, the use device, DNA purification tube into the centrifugal tube, DNA purification pipe is lengthways and transverse bug is a pipe just buckled, time is convenient to operate, and can avoid the pollution.
NOVELTY - A fertilizer is formed based on fish by decomposing or grinding fish parts into fish paste; depositing the fish paste into a tank; injecting air into the tank to form bubbles to agitate the fish paste and to accelerate its decomposition; and adding acid to the fish paste after fermenting to form the fertilizer.    USE - Method for forming fertilizer based on fish (claimed).    ADVANTAGE - The method produces fertilizer from fish that is highly concentrated, yet retains natural micro and macro nutrients of the fish. The resulting fertilizer is concentrated to reduce transportation cost. The use of aerator or micro-bubble generator provides large amounts of oxygen to the fermentation process so that the fermentation occurs as rapidly as possible; mixes the liquid to ensure that fish, microorganisms, and oxygen are widely distributed; and avoids the need for a separate mechanical agitator to prevent sediment from accumulating on the bottom of the tank. The method produces inexpensive fertilizers, and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system to make fertilizer based on fish comprising food compost machine (10) to receive fish parts, mix the fish parts with a base of bio-chips, and facilitate growth of microorganisms with the bio-chips and oxygen; and tank receiving the fish paste from the food compost machine.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view showing system used to make fish fertilizers.    Source fish (01)    Compost machine (10)    Microorganisms and enzymes (13)    Water (14)    Pump (15)
NOVELTY - Preparation of substituted 2-ethylaminopyridine derivative (III) involves hydrogenating substituted 2-methyl cyanopyridyl derivative (II) in presence of metal catalyst, catalyst modifier, and acid.    USE - Preparation of substituted 2-ethylaminopyridine derivative e.g. 2-(3-chloro-5-(trifluoromethyl)pyridin-2-yl)ethanamine, for producing N-(2-(pyridin-2-yl)ethyl)benzamide derivative e.g. (N-(2-(3-chloro-5-(trifluoromethyl)-2-pyridinyl)ethyl)-2-(trifluoromethyl)benzamide) (all claimed), used as fungicide.    ADVANTAGE - The method enables safe, environmentally-friendly and economical preparation of substituted 2-ethylaminopyridine derivative with high selectivity.    DETAILED DESCRIPTION - Preparation of substituted 2-ethylaminopyridine derivative of formula (III) and its salt involves hydrogenating substituted 2-methyl cyanopyridyl derivative of formula (II) in presence of metal catalyst, catalyst modifier, and acid.    p=1-4;and    X=halo or 1-4C (halo)alkyl.    An INDEPENDENT CLAIM is included for production of N-(2-(pyridin-2-yl)ethyl)benzamide derivative of formula (I), which involves reacting 2-ethylaminopyridine derivative (III) with benzoyl halide of formula (IV).    Hal=fluoro, chloro or bromo;    q=1-4;    Y'=X.
NOVELTY - Preparation of water-soluble indomethacin salt involves adding basic compound to mixture of indomethacin and water at 0-100 degrees C, controlling pH of the solution to 6-14, reacting indomethacin with a basic compound in aqueous solution for 2-10 hours, crystallizing, filtering, collecting filter cake, and drying.    USE - Preparation of water-soluble indomethacin salt (claimed).    ADVANTAGE - The method enables simple, economical, efficient and environmentally-friendly preparation of water-soluble indomethacin salt having high purity with high yield.
NOVELTY - Separation of ionic liquid involves separating (3, 4) an ionic liquid from a solution containing an ionic liquid using an ion-exchange membrane.    USE - Separation of ionic liquid used as enzyme saccharification pre-processing agent of cellulose biomass.    ADVANTAGE - The method enables effective separation of ionic liquid and saccharide after pre-processing biomass and saccharification process using ionic liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining production of ethanol. (Drawing includes non-English language text)    Pre-processing of biomass (1)    Saccharification process (2)    Separation process (3,4)
NOVELTY - Windproof sand-fixing plant seedling matrix comprises municipal sludge and biomass carbon. The seedling matrix is prepared by aerobically composting municipal sludge and biomass carbon.    USE - Windproof sand-fixing plant seedling matrix used for drought desert area and grass-planting forestation.    ADVANTAGE - The seedling matrix is rich in organic matter and nitrogen-phosphorus-potassium, has strong microbial activity, and develops root system. The method has short transplanting period and increases survival rate.
NOVELTY - Eggplant seedling special matrix comprises organic mixture, grass peat, perlite, vermiculite, plant ash, and inorganic fertilizer.    USE - Eggplant seedling special matrix.    ADVANTAGE - The special matrix has light texture, full nutrition, water content of less than or equal to 50%, organic matter content (dry basis) of greater than or equal to 20%, total nutrient content of 1-5%, bulk density of 0.2-0.6 g/cm3, total porosity of 60-80%, gas-water ratio of 1:2-4, emulsifiable concentrate value of 1-3.5 mS/cm, and pH of 5.5-7.5. The method has low cost.
NOVELTY - A composite material comprises 56-75 wt.% rice hull, 13-30 wt.% diatomite, 5.5-9.5 wt.% polyaluminum chloride, and 3.5-7.5 wt.% enzyme bacteria in which enzyme bacteria comprise Bacillus subtilis, yeast, and actinomycete, B. subtilis has effective viable count of 2000000000/g, yeast has effective viable count of 3500000/g, and actinomycete has effective viable count of 3000000/g.    USE - A composite material for treatment of municipal wastewater (claimed).    ADVANTAGE - Process is simple, and product removes degraded organic matter, phosphorus, and nitrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of composite material which involves uniformly mixing rice hull and enzyme bacteria, naturally stacking, fermenting at 65-70 degrees C for 2 weeks to obtain mixed raw material, uniformly mixing mixed raw material, water, and brown sugar having weight ratio of 1:0.3:0.01, fermenting for 110-130 minutes, treating sewage at less than or equal to 10 degrees C, and uniformly mixing fermented mixed raw material, diatomite, and polyaluminum chloride; and    (2) treatment of municipal wastewater which involves uniformly mixing mixed raw material, water, and brown sugar, fermenting for 2 hours, treating sewage at less than or equal to 10 degrees C, uniformly mixing fermented mixed raw material, diatomite, and polyaluminum chloride to obtain composite material, and putting into oxic (O) part of municipal wastewater anoxic/oxic (A/O) system in which addition amount of wastewater is 0.2-0.45 kg/ton.
NOVELTY - Method for processing sludge using microbial composition, involves (a) subjecting sludge to fermentation, (b) mixing fermented sludge with dried sludge, (c) mixing sludge mixture obtained in step (b) with conditioning agent, (d) preparing nutritional solution containing wheat bran, (e) mixing the nutritional solution with microbial composition, (f) uniformly mixing products obtained in steps (c) and (e), and (g) stirring mixture obtained in step (f). The conditioning agent comprises agricultural straw powder, mushroom residue, sawdust and livestock manure.    USE - The method is useful for processing sludge using microbial composition (claimed) which is used as building material or biological fuel.    ADVANTAGE - The method is cost-effective to perform and suitable for industrial operation, and has low failure rate.    DETAILED DESCRIPTION - Method for processing sludge using microbial composition, involves (a) subjecting sludge to fermentation, and regulating moisture content of fermented product at 70-75%, (b) mixing fermented sludge with dried sludge in a volume ratio of 1:1-2, (c) mixing sludge mixture obtained in step (b) with conditioning agent in a ratio of 600-800:400-200, (d) preparing nutritional solution comprising wheat bran, cellulose and stabilizing agent in a ratio (in wt.%) of 85:10:5, (e) mixing the nutritional solution with microbial composition in a weight ratio of 1-2:1-2, and uniformly stirring obtained mixture, (f) uniformly mixing products obtained in steps (c) and (e) in a weight ratio of 600-800:1-2, and (g) stirring mixture obtained in step (f) for 8-10 days. The conditioning agent comprises agricultural straw powder, mushroom residue, sawdust and 15-30 wt.% livestock manure. The microbial composition comprises VT microbes.
NOVELTY - Producing methanol, formaldehyde or greater than or equal to 2C hydrocarbon, comprises (a) processing mixed gas containing methane, oxygen and inert gas with plasma, (b) performing methane conversion reaction in the presence of catalyst based on the plasma processed of mixed gas, and (c) circulating the inert gas to the step (a) by recovering through a separation membrane from the obtained reaction product. The step (a) and the step (b) are carried out sequentially or simultaneously.    USE - The method is useful for producing methanol, formaldehyde or greater than or equal to 2C hydrocarbon (claimed).    ADVANTAGE - The method is economical as it utilizes the adsorption heat generated while removing water from the reaction product, reuses the inert gas, produced product of high purity, increases methane conversion by using a gas separation membrane module, and utilizes the inert gas as a carrier gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for methane conversion device comprising a first unit for processing the mixed gas containing methane, oxygen and inert gas with low temperature non-thermal plasma, a second unit for performing methane conversion reaction in the presence of catalyst based on the plasma processed of mixed gas, a third unit for recovering the inert gas through the separation membrane from the reaction product discharged from the second unit, and a fourth unit for circulating the inert gas recovered from the third unit. The first unit and second unit is each independently a distinct unit or an integrated unit.
NOVELTY - The portable fuel cell system comprises a display unit (40), a valve for controlling the fuel for the combustion and a conduction detection sensor (60) for converting the electricity generated with a fuel cell unit (10). A battery (30) is charged with electricity supplied from a direct current output unit (20). A necessary warning signal is displayed on the display unit in the emergency shut-down of the system. A control unit (50) stops the operation of the fuel cell unit.    USE - Portable fuel cell system.    ADVANTAGE - The portable fuel cell system comprises a display unit, a valve for controlling the fuel for the combustion and a conduction detection sensor for converting the electricity generated with a fuel cell unit, and hence ensures enhanced safety of fuel cell system, where efficient operation of the fuel cell system is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an emergency shut-down control method for a portable fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the portable fuel cell system.    Fuel cell unit (10)    Direct current output unit (20)    Battery (30)    Display unit (40)    Control unit (50)    Conduction detection sensor (60)
NOVELTY - The preparation method of a biomass-based adhesive involves mixing 100 pts. wt. biomass-based polyols, 1-15 pts. wt. chain extenders, 20-50 pts. wt. modifying agent and 10-30 pts. wt. tackifier resin, dehydrating, then adding 40-80 pts. wt. isocyanate, 0.01-2 pts. wt. catalyst and 1-30 pts. wt. modifier in an inert gas atmosphere, and reacting at 30-60 degrees C for 1-4 hours.    USE - Method is useful for preparing biomass-based adhesive (claimed).    ADVANTAGE - The method provides environmentally-friendly adhesive having excellent heat stability and performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass-based adhesive obtained by the method.
NOVELTY - Dry fermentation test reactor comprises fermentation tank, top cover (6), slurry tank (5), and constant-temperature heating device (8) in which fermentation tank contains outer tank body (1), inner tank body (2), vacuum chamber (3), heat insulating cotton (10), filter plate (4), slurry outlet, biogas pressure balance port (6a), biogas slurry inlet (6b), and spiral spray head (9).    USE - A dry fermentation test reactor.    ADVANTAGE - Dry fermentation test reactor is safe and easy to control and filter liquid is easy to separate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of dry fermentation test reactor.    Outer tank body (1)    Inner tank body (2)    Vacuum chamber (3)    Filter plate (4)    Biogas slurry tank (5)    Top cover (6)    Pressure balance port (6a)    Biogas slurry inlet (6b)    Constant-temperature heating device (8)    Spiral spray head (9)    Heat insulating cotton (10)
NOVELTY - Polysaccharide/gliadin composite film, is claimed. The polysaccharide is curdlan or konjac glucomannan. The gliadin is wheat gliadin or corn gliadin.    USE - The composite film is useful as a food packaging film material and food or drug delivery material.    ADVANTAGE - The composite film is smooth, non-toxic, and environmental friendly; has good mechanical, and barrier properties, and good water vapor transmission rate, oxygen transmission rate and good light transmittance effect, and sustained-releasing effect; and can naturally degrade rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing composite film, comprising (i) stir polysaccharide by adding distilled water for 30-180 minutes at 25-90 degrees C by placing in a water bath, to obtain polysaccharide sol-gel; (ii) stirring gliadin by adding 50-90% ethanol solution at 25-50 degrees C for 10-30 minutes, to obtain gliadin solution; and (iii) mixing the product obtained in the steps (i) and (ii), stirring by placing the mixture in water bath at 25-90 degrees C for 30-90 minutes, completely mixing, to obtain a mixed dispersion system, and casting film, drying, and taking out the film, to obtain the product.
NOVELTY - A carbon dioxide/methane-separation metal-organic framework structure film material contains alpha -alumina as carrier, and 3-isocyanate propyltriethoxysilane modified CAU-1-type film on carrier surface. The 3-isocyanate propyltriethoxysilane modified CAU-1-type film is obtained by linking together cyano group-containing 3-isocyanate propyltriethoxysilane and amino group-containing CAU-1-type agent.    USE - Metal-organic framework structure film is used for separation of mixed gas containing carbon dioxide and methane (claimed).    ADVANTAGE - The carbon dioxide/methane-separation metal-organic framework structure film has high density.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of carbon dioxide/methane-separation metal-organic framework structure film material.
NOVELTY - Biological zinc organic foliar fertilizer comprises 1000-3000 pts. wt. water hyacinth, 1-3 pts. wt. zinc sulfate, 0.5 pt. wt. bran solid fermentation bacteria, 0.2 pt. wt. Aspergillus mauve and 0.3 pt. wt. Saccharomyces cerevisiae yeast.    USE - Biological zinc organic foliar fertilizer.    ADVANTAGE - The fertilizer has simple preparation, low device investment and low raw material cost. It utilizes agricultural wastewater.    DETAILED DESCRIPTION - Biological zinc organic foliar fertilizer comprises 1000-3000 pts. wt. water hyacinth, 1-3 pts. wt. zinc sulfate, 0.5 pt. wt. bran solid fermentation bacteria, 0.2 pt. wt. Aspergillus mauve and 0.3 pt. wt. Saccharomyces cerevisiae yeast. The fertilizer is prepared by digging pond in farmland, collecting agricultural wastewater or animal excretion liquid after irrigation, adding zinc sulfate, cultivating water hyacinth, taking 2/3 of mature product every 7 days; taking out water hyacinth, pulverizing into 40 meshes fine powders, adding into high temperature and high speed fermentation kettle, adding solid fermentation bacteria, fermenting for 12 hours; continue fermenting in glass fermentation kettle, adding water, Aspergillus mauve and Saccharomyces cerevisiae yeast, fermenting for 7 days; and screening through 400 meshes screen, and taking filter liquid residue.
NOVELTY - Synthesis of 2,5-dicholorophenol (I) comprises reacting 2,5-chloroaniline (II) with methyl nitrite under acidic condition, and steam distilling.    USE - Method for synthesizing 2,5-dicholorophenol (I) used as key intermediate of dicamba (claimed).    ADVANTAGE - The method is simple and suitable for industrialization, and has low pollution, and low cost.    DETAILED DESCRIPTION - Synthesis of 2,5-dicholorophenol of formula (I) comprises reacting 2,5-chloroaniline of formula (II) with methyl nitrite under acidic condition, and steam distilling.
NOVELTY - A benzoin oxime derivative (I) is new.    USE - Benzoin oxime derivative used for producing chemicals and clinical medicine.    DETAILED DESCRIPTION - A benzoin oxime derivative of formula (I) is new.    E1, E2=CO2R;    R=straight-chain or branched chain alkyl, unsaturated hydrocarbon, or aromatic hydrocarbon; and    R1, R2=H, straight or branched chain alkyl, halo, or alkoxy.    An INDEPENDENT CLAIM is included for the preparation of compound (I).
NOVELTY - Xylene is added to reactor, pyridine base mixture is passed to reactor through funnel, and stirred uniformly. The reactor is heated to 80-135 degrees C, refluxed and dehydrated. The resulting mixture is cooled to room temperature, sodium amide is added to reactor, stirred, and refluxed. Water droplets are added to reactor, stirred, hydrolyzed, stirring is stopped, and the reaction mixture is maintained, layer-separated, and xylene as aqueous phase is removed to obtain aminopyridine as organic phase. The mass ratio of xylene and pyridine base mixture is (2-3):1.    USE - Synthesis of aminopyridine from pyridine base mixture (claimed).    ADVANTAGE - The method provides aminopyridine by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Xylene is added to reactor, pyridine base mixture is passed to reactor through funnel, and stirred uniformly. The reactor is heated to 80-135 degrees C, refluxed and dehydrated. The resulting mixture is cooled to room temperature, sodium amide is added to reactor, stirred, and refluxed. Water droplets are added to reactor, stirred, hydrolyzed, stirring is stopped, and the reaction mixture is maintained, layer-separated, and xylene as aqueous phase is removed to obtain aminopyridine as organic phase. The mass ratio of xylene and pyridine base mixture is (2-3):1. The mass ratio of sodium amide and pyridine base mixture is 1:(1-1.5). The mass ratio of water and pyridine base mixture is 1:(2-3). An INDEPENDENT CLAIM is included for separation and purification method of aminopyridine from pyridine base mixture.
NOVELTY - Extracting tea polyphenol involves utilizing percolation method, where solvent is mixed with tea to obtain tea polyphenol. The tea residue is further processed to obtain tea polyphenol.    USE - Method for extracting tea polyphenol (claimed).    ADVANTAGE - The method enables to extract pure tea polyphenol in simple, practical, safe, low cost and eco-friendly manner, ensuring suitability for industrial production.
NOVELTY - Traditional Chinese medicine comprises 0.3-0.6 pt. wt. gypsum, 0.8-1.6 pts. wt. Uncaria, 0.6-1.5 pts. wt. rhizoma anemarrhenae, 0.4-1.2 pts. wt. Rhaponticum uniflorum, 0.8-1.2 pts. wt. rhizoma aspidistrae, 0.6-1.5 pts. wt. Manglietia fruit, 1-1.5 pts. wt. vinblastine flower, 1-2 pts. wt. kudzu root, 0.8-1.2 pts. wt. Cynanchum paniculatum, 0.8-1.2 pts. wt. fructus momordicae, 0.3-0.6 pt. wt. flos sophorae and 0.5-1.2 pts. wt. Schizonepeta tenuifolia.    USE - Traditional Chinese medicine in the form of extract, powder, pill or ointment used for treating suppurative tonsillitis (claimed).    ADVANTAGE - The medicine is simple and convenient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of traditional Chinese medicine extract comprising washing gypsum, drying, grinding, adding water, stirring, decanting, standing, adding wheat brain and remaining ingredients, heating for 15-30 minutes, cooling, adding boiling water, simmering for 40-60 minutes, adding cooking oil, heating for 50-70 minutes, cooling, crushing, soaking in alcohol for 20 minutes, filtering, recovering alcohol, mixing, sterilizing and packaging;    (2) preparation of traditional Chinese medicine powder comprising washing gypsum, drying, crushing, adding water, mixing, grinding, decanting, drying, mixing remaining raw materials, degreasing, grinding and sieving;    (3) preparation of traditional Chinese medicine pill comprising washing gypsum, drying, grinding, adding water, stirring, decanting, standing, adding wheat brain and remaining ingredients, heating for 23 minutes, degreasing, grinding, mixing, sieving, adding honey and encapsulating; and    (4) preparation of traditional Chinese medicine ointment comprising washing gypsum, drying, grinding, adding water, stirring, decanting, drying, mixing remaining raw materials, adding wheat brand soaking in boiling water for 40-55 minutes, simmering for 50 minutes, filtering, mixing, heating and concentrating.
NOVELTY - Producing biogas in a biogas reactor, comprises: e.g. providing at least a quantitative deficit feature, based on the biomass of a specific biogas reactor; indicating at least one measurement method for the measurement of at least one deficit feature; determining at least one reference value for at least one deficit feature; and producing biogas in the biogas reactor; determining at least one value of deficit feature in the biomass from the biogas reactor by measurement method; providing at least one quantitative selection criterion for selecting at least one enzyme-containing preparation.    USE - The method is useful for producing biogas in a biogas reactor (claimed).    ADVANTAGE - The method: provides improved supply of enzymes to biogas reactor; and ensures measurement of the specific biogas formation in simple manner.    DETAILED DESCRIPTION - Producing biogas in a biogas reactor, comprises: providing at least a quantitative deficit feature, based on the biomass of a specific biogas reactor; indicating at least one measurement method for the measurement of at least one deficit feature; determining at least one reference value for at least one deficit feature; and producing biogas in the biogas reactor; determining at least one value of at least one deficit feature in the biomass from the biogas reactor by at least one measurement method; providing at least one quantitative selection criterion for selecting at least one enzyme-containing preparation from at least two enzyme-containing preparations; and adding the enzyme-containing preparations at least in an amount or for a period of biomass in the biogas reactor, until the measured error disappears, if the determined deficit feature value in the biomass of at least one determined and provided guideline differs.
NOVELTY - Mutual growth promotion and conversion of giant juncao-straw mushroom-fertilizer by providing shade straw mushroom by growing giant juncao, photosynthesizing, producing carbon dioxide, and promoting growth with waste material as bioorganic fertilizer.    USE - Method for mutual growth promoting and converting giant juncao-straw mushroom-fertilizer (claimed).    ADVANTAGE - The method shortens growth period for 1-2 days, increases biological efficiency at 3-5% and giant juncao yield at 68%, and has good economic and ecological effect.
NOVELTY - Processing a residual product originating from a fermenter reactor as a mash substrate for solid or solid-containing organic biomass for biogas generation, comprises carrying out solid-liquid separation of the residue, supplying the liquid fraction as thin overflow into an insulated reaction container, subjecting the thin overflow to anaerobic ammonium oxidation using anammox organisms, maintaining the coenosis of the reaction container to a temperature of 35-45 degrees C, mixing nitrogen rich substrate for biogas fermentation, and supplying together with this into the first stage of biogas process.    USE - The method is useful for processing residual product originating from fermenter reactor as mash substrate for solid or solid-containing organic biomass for biogas generation.    DETAILED DESCRIPTION - Processing a residual product originating from a fermenter reactor as a mash substrate for solid or solid-containing organic biomass for biogas generation, comprises carrying out solid-liquid separation of the residue, supplying the liquid fraction as a thin overflow into an insulated reaction container, subjecting the thin overflow to anaerobic ammonium oxidation using anammox organisms to reduce the ammonia concentration in the submersion process, maintaining the coenosis of the reaction container to a temperature of 35-45 degrees C, mixing nitrogen rich substrate as process water of a biomass for biogas fermentation after a residence time in the reaction container, and supplying together with this into the first stage of a biogas process.
NOVELTY - Levulinic acid is separated from biomass hydrolysate by optionally solid-liquid-separating biomass hydrolysate to yield solid and liquid fractions, optionally subjecting biomass hydrolysate or liquid fraction to solvent-solvent extraction to yield organic phase containing levulinic acid and aqueous phase, recovering organic phase, distilling biomass hydrolysate, liquid fraction, or organic phase to distillation to give distillate containing levulinic acid and distillation residue, adding base to distillation residue, optionally cooling distillation residue, and recovering distillation residue.    USE - Separation of levulinic acid from biomass hydrolysate (claimed).    ADVANTAGE - The process gives a flowable distillation residue even after cooling, making it easier to discharge the residue for use as, e.g. black liquor. High levulinic acid yields are higher because addition of levulinic acid to residue is no longer necessary to keep the residue flowable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of distillation residue obtainable from separation process of levulinic acid as energy source in a paper plant.
NOVELTY - The system has briquetting arrangement (12) for briquetting derived boiler and electrostatic precipitator ash (24) from fluidized bed combustion unit (1) with steam generator (2) and subsequent electrostatic precipitator (3). A coke fired Mephrec (RTM: metallurgical phosphor recycle) reactor (14) has a fan (15) for transporting the fuel gas (25) generated in the fluidized bed combustion unit. Granulation equipment (16) is provided for granulating phosphorus slag from reactor.    USE - Complete system for utilization of phosphorus-containing waste in incinerator such as mono-incineration plants for sewage sludge and/or meat and bone meal, in power plants or in supplementary firing in kilns in cement industry and plant for gassing of material and energy recycle of phosphorus-containing waste by air and/or oxygen gasification melting in metallurgical furnaces.    ADVANTAGE - The phosphorus-containing waste is recycled in economic manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the complete system for utilization of phosphorus-containing waste.    Fluidized bed combustion unit (1)    Steam generator (2)    Electrostatic precipitator (3)    Briquetting arrangement (12)    Mephrec reactor (14)    Fan (15)    Granulation equipment (16)    Electrostatic precipitator ash (24)    Fuel gas (25)
NOVELTY - Biogas plant (10) comprises at least one biogas reactor (11) in which a gaseous product is prepared, and at least one filter device (14) which filters useful material out of the gaseous product from the biogas plant and/or from at least one biogas reactor. The filter device comprises biocarbon which accumulates useful material.    USE - Used as a biogas plant.    ADVANTAGE - The biogas plant ensures lasting viability of useful material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device for collecting valuable substances with a filter device, comprising biocarbon, which is adapted to accumulate useful material;    (2) a device for producing biocarbon, comprising carbonization device (18) which is adapted to carbonize digestate from biogas plant;    (3) producing biocarbon, comprising converting fermentation residues from a biogas plant to biocarbon; and    (4) operating a biogas plant, comprising providing a gaseous product in at least one biogas reactor of the biogas plant, filtering and collecting recyclable materials from the gaseous product using filter device, where recyclable material is accumulated on the biocarbon, and carbonizing of fermentation residues of biogas plant to produce biocarbon.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Biogas plant (10)    Biogas reactor (11)    Hydrolysis reactor (12)    Fermentation reactor (13)    Filter device (14)
NOVELTY - An on-board hydrogen is generated to produce hydrogen-enriched compressed natural gas (HCNG) used for compressed natural gas (CNG) power vehicles.    USE - Generation of on-board hydrogen for production of hydrogen-enriched compressed natural gas used for compressed natural gas power vehicles (all claimed).    ADVANTAGE - Generation process has low cost. System minimizes combustion emissions and optimizes engine performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system (10) with on-board motor vehicle (12) for production of HCNG alternative fuel comprising partial oxidation (POX) reformer (22), steam reformer (24), carbon dioxide reformer (26), high-temperature water gas shift reformer, low-temperature water gas shift reformer, reforming system control (14) synchronized with engine controls unit (ECU) (18) to produce calibrated ratios of hydrogen in HCNG alternative fuel, and ECU configured to operate with variable hydrogen gas ratios in HCNG alternative fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of an on-board vehicle system for producing hydrogen-enriched natural gas fuel.    System (10)    On-board motor vehicle (12)    Reforming system control (14)    Engine controls unit (18)    Partial oxidation reformer (22)    Steam reformer (24)    Carbon dioxide reformer (26)
NOVELTY - A metal-supported zeolite molded product is formed by molding zeolite by which the metal component is supported, and contains 0.5-7 %mass sodium oxide with respect to metal-supported zeolite molded product. The metal component is chosen from silver, copper, zinc, nickel, iron, cerium, lanthanum, zirconium and titanium.    USE - Metal-supported zeolite molded product is used for adsorption agent for removing sulfur, sulfide and mecaptan from dimethyl-ether fuel and hydrocarbon fuel e.g. LPG, town gas, natural gas, naphtha, kerosene oil, light oil, ethane, ethylene, propane, propylene, butane and butene in production of hydrogen used in fuel cell system (all claimed).    ADVANTAGE - The metal-supported zeolite molded product efficiently removes the sulfur compound contained in hydrocarbon fuel or dimethyl-ether fuel at room temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of metal-supported zeolite molded product; and    (2) manufacture of hydrogen, which involves de-sulfurizing hydrocarbon fuel or dimethyl-ether fuel, and contacting desulfurized fuel with partial oxidation modification catalyst, auto-thermal reforming catalyst, and steam-reforming catalyst.
NOVELTY - A silkworm excrement vertical continuous fermentation system comprises tank (1), reservoir (2), feed control board (3), temperature guide (5), bottom plate (6), discharge port (9), discharge control board (8), motor (7), and fixed foot (10).    USE - Silkworm excrement vertical continuous fermentation system.    ADVANTAGE - The fermentation system does not pollute the environment, and it has simple structure, easy operation, low cost, and small floor area.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of silkworm excrement vertical continuous fermentation system.    Tank (1)    Reservoir (2)    Feed control board (3)    Temperature guide (5)    Bottom plate (6)    Motor (7)    Discharge control board (8)    Discharge port (9)    Fixed foot (10)
NOVELTY - The device has an insect trapping device (3) comprisng the housing (31) provided with a liquid storage chamber (33) whose top portion is provided with a spray nozzle (34). A timer (4) is connected with a processor (6) through a driver (5). A control valve is connected with a bait bowl (36) at bottom of storage chamber. The electric storage box (7) and solar panels (8) are fixed at top portion of support. The solar panels are connected with electric storage box. An insect killing section is connected with a vertical guide rail (310). A small air cylinder (312) is controlled by processor.    USE - Device for deinsectization of forest using insecticidal fluid.    ADVANTAGE - The structure of the device is simplified, the use stability of the device is improved. The insecticidal effect of the device is improved, and the environmental pollution is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the forest deinsectization device.    Insect trapping device (3)    Timer (4)    Driver (5)    Processor (6)    Electric storage box (7)    Solar panel (8)    Housing (31)    Liquid storage chamber (33)    Spray nozzle (34)    Bait bowl (36)    Vertical guide rail (310)    Small air cylinder (312)
NOVELTY - Fertilizer comprises 2-5 pts. wt. alpha-terpineol, 5-10 pts. wt. 25% azoxystrobin wettable powder, 5-10 pts. wt. tea, 30-40 pts. wt. inorganic fertilizer, 8-18 pts. wt. microelement, 10-20 pts. wt. filler and 5-60 pts. wt. organic fertilizer.    USE - Fertilizer used for preventing and treating Eucalyptus leaves blight (claimed).    ADVANTAGE - The fertilizer has high efficiency and no residue.
NOVELTY - Gentiopicroside (I) is new.    USE - Gentiopicroside.    ADVANTAGE - The method enables increase yield of gentiopicroside and does not use organic solvent.    DETAILED DESCRIPTION - Gentiopicroside of formula (I) is new. An INDEPENDENT CLAIM is included for a method for preparing gentiopicroside.
NOVELTY - This utility new type claims a one organic fertilizer stacking, a walking wheel below four crossing comprises a fermentation pool is walking, the walking vehicle comprises vehicle frame and a frame, the four walking front of rear two rows of wheel set, two walking wheel of interference connection manner to install in the first two end rotating shaft, a first rotating shaft by mounting in a vehicle frame of electric machine drive, a first rotating shaft axial direction are cloth has a multi-turning mechanism, a stirring claw the multi-turning mechanism set by the first rotating shaft outside and b and the same rotating shaft set and a shaft set the circumferential direction of one cloth. The first rotating shaft a table motor driving walking wheel and walking and walking wheel are rotating at the same time of stirring claw drives the overturning up and down, realize the one machine, a simple structure, a convenient to use.
NOVELTY - A calcium salicylate is prepared by distilling hydrocarbyl salicylic acid, adding salicylaldehyde, heating with mixture containing volatile solvent oil, base oil, lime, and accelerator at 40-80 degrees C, adding surfactant and alkyl salicylic acid, stirring at 60-80 degrees C for 30-40 minutes, cooling to 50-54 degrees C, adding hydrocarbon accelerant and catalyst under carbon dioxide gas atmosphere, reacting to obtain stable colloidal dispersion, removing volatile solvent oil, accelerator and water, adding filter aid, and filtering.    USE - Method for preparing calcium salicylate (claimed).    ADVANTAGE - The method is nontoxic, and environment-friendly.
NOVELTY - A 4-chloro-phenyl butane is synthesized by taking butane and 1,4-dichlorobenzene as solvent, adding catalyst, reacting, adding ice and concentrated hydrochloric acid, extracting, drying, vacuum distilling, adding p-phenylene-butoxy benzoic acid methyl ester, dimethylformamide, methylparaben, potassium carbonate, sodium bromide and triethylbenzylammonium chloride, reacting, cooling, adding water, extracting with dichloromethane, removing dichloromethane, adding sodium hydroxide solution and ethanol, refluxing, distilling with ethanol, adjusting pH value, precipitating, filtering, and drying.    USE - Method for preparing 4-chloro-phenyl butane (claimed).    ADVANTAGE - The method is cheap, easy, short, low-cost, safe, environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - A 4-chloro-phenyl butane is synthesized by taking butane and 1,4-dichlorobenzene as solvent at molar ratio of 1:0.2-0.5, adding catalyst, reacting at 115 degrees C, adding ice and concentrated hydrochloric acid at volume ratio of 5:1, extracting, drying, vacuum distilling to obtain 4-phenyl-chlorobutane, adding p-phenylene-butoxy benzoic acid methyl ester, dimethylformamide, methylparaben, potassium carbonate, sodium bromide and triethylbenzylammonium chloride, reacting at 50 degrees C for 11 hours, cooling to room temperature, adding water, extracting with dichloromethane, removing dichloromethane under reduced pressure, adding 15% sodium hydroxide solution and ethanol, refluxing for 3-4 hours, distilling with ethanol, adjusting pH value to 2, precipitating to obtain white solid, filtering, and drying.
NOVELTY - Preparation of resveratrol phospholipid compound microemulsion granules comprises mixing surfactant, octanoic acid/capric acid triglyceride and co-emulsifier to obtain blank microemulsion; taking resveratrol phospholipid compound, adding blank micro-emulsion, stirring to obtain uniform transparent resveratrol microemulsion; taking hydroxypropyl methylcellulose, adding resveratrol microemulsion, stirring and mixing uniformly to obtain suspension-shaped resveratrol microemulsion; and mixing with microcrystalline cellulose, grinding, granulating and sieving.    USE - Method for preparing resveratrol phospholipid compound microemulsion granules (claimed).    ADVANTAGE - The method is simple, does not need high energy consumption, increases solubility in water, and increases of stomach and intestinal channel lipolytic dispersion and biological active use.    DETAILED DESCRIPTION - Preparation of resveratrol phospholipid compound microemulsion granules comprises mixing 100 pts. wt. surfactant, 5-30 pts. wt. octanoic acid/capric acid triglyceride and 1-40 pts. wt. co-emulsifier at 40-60 degrees C to obtain blank microemulsion; taking 3 pts. wt. resveratrol phospholipid compound, adding 12-57 pts. wt. blank microemulsion, stirring to obtain uniform transparent resveratrol microemulsion at 40-60 degrees C; taking 1 pt. wt. hydroxypropyl methylcellulose, adding 9-49 pts. wt. resveratrol micro-emulsion, stirring and mixing uniformly to obtain suspension-shaped resveratrol microemulsion at 40-60 degrees C; and taking 1-3 pts. wt. microcrystalline cellulose, adding 1 pt. wt. suspension-shaped resveratrol microemulsion, uniformly mixing, grinding, granulating and sieving.
NOVELTY - Preparation of potato starch factory filter sludge fertilizer comprises drying filter sludge, adding conditioning agents, adjusting pH to 6-7, mixing, reacting, stacking and granulating. Conditioning agent is calcium superphosphate, triple superphosphate, enriched superphosphate, ammoniated superphosphate, calcium magnesium phosphate, steel slag phosphate fertilizer, defluorinated phosphate fertilizer, fuel ash, ammonium bicarbonate, ammonium sulfate, ammonium carbonate, sulfurized ammonium phosphate, ammonium phosphate, dibasic calcium phosphate, sucrose, calcium carbonate and/or lime.    USE - Method for preparing potato starch factory filter sludge fertilizer (claimed).    ADVANTAGE - The preparation method is environment-friendly and economical.    DETAILED DESCRIPTION - Preparation of potato starch factory filter sludge fertilizer comprises drying filter sludge, adding conditioning agents, adjusting pH to 6-7, mixing, reacting, stacking and granulating. Conditioning agent is calcium superphosphate, triple superphosphate, enriched superphosphate, ammoniated superphosphate, calcium magnesium phosphate, steel slag phosphate fertilizer, defluorinated phosphate fertilizer, fuel ash, ammonium bicarbonate, ammonium sulfate, ammonium carbonate, sulfurized ammonium phosphate, ammonium phosphate, dibasic calcium phosphate, sucrose, calcium carbonate, lime, calcium phosphate, rare-earth elements, somatomedin and trace elements.
NOVELTY - Pomegranate fertilizer comprises 15-17 pts. wt. nitrogen fertilizer, 10-12 pts. wt. phosphate fertilizer, 12-14 pts. wt. potash fertilizer, 80-100 pts. wt. chicken manure, 20-30 pts. wt. weathered coal, 10-12 pts. wt. phosphate powder, 20-30 pts. wt. potassium mineral powder, 10-12 pts. wt. yellow bean cake, 70-90 pts. wt. rice husk powder, 3-5 pts. wt. bacterial species powder, 60-80 pts. wt. of bentonite and 50-60 pts. wt. of water.    USE - Pomegranate fertilizer (claimed).    ADVANTAGE - The pomegranate fertilizer provides green organic fruit with required nutrients, enhances the crop production and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of pomegranate fertilizer.
NOVELTY - A fertilizer comprises 15-25 pts. wt. photosynthetic liquid microbial inoculum, 3-5 pts. wt. fulvic acid, 10-12 pts. wt. urea, 4-6 pts. wt. diammonium phosphate, 8-10 pts. wt. potassium sulfate, 1-3 pts. wt. potassium silicate, 2-4 pts. wt. magnesium sulfate, 12-14 pts. wt. calcium superphosphate, 10-12 pts. wt. radix aconiti agrestis, 20-30 pts. wt. corn straw powder, 17-19 pts. wt. Sesbania, 20-22 pts. wt. Chinese trumpet creeper, 7-9 pts. wt. cottonseed extract and 8-10 pts. wt. tea seed extract.    USE - Fertilizer is used for Litchi.    ADVANTAGE - The fertilizer is environmentally-friendly, has excellent disease prevention effect and rapid effect, and improves soil quality and yield of Litchi.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for predation of fertilizer.
NOVELTY - A coated fertilizer contains 40-45 pts. wt. wood chips, 53-55 pts. wt. cow dung, 2-3 pts. wt. gypsum powder, 1-3 pts. wt. rosin, 0.5-0.8 pt. wt. borax, 6-8 pts. wt. urea, and 4-6 pts. wt. soil improving agent. The soil improving agent contains 10-15 pts. wt. zinc sulfate, 10-15 pts. wt. medical stone, 0.2-0.3 pt. wt. nanocarbon powder, 1-2 pts. wt. KH-550 (RTM: ( gamma )-aminopropyltriethoxysilane), 10-12 pts. wt. ferrous sulfate, 3-6 pts. wt. chlorinated paraffin, 0.3-0.6 pt. wt. selenium yeast, 1-2 pts. wt. oyster shell nanopowder, 1-2 pts. wt. borax, and 2-3 pts. wt. chitosan sugar.    USE - Coated fertilizer is used for strawberry flowering.    ADVANTAGE - The coated fertilizer ensures excellent nutrition balance, increases the strawberry flowering and improves yield of strawberries.    DETAILED DESCRIPTION - Coated fertilizer contains 40-45 pts. wt. wood chips, 53-55 pts. wt. cow dung, 2-3 pts. wt. gypsum powder, 1-3 pts. wt. rosin, 0.5-0.8 pt. wt. borax, 6-8 pts. wt. urea and water. The soil improving agent contains 10-15 pts. wt. zinc sulfate, 10-15 pts. wt. medical stone, 1-2 pts. wt. KH-550 (RTM: ( gamma )-aminopropyltriethoxysilane), 10-12 pts. wt. ferrous sulfate, 3-6 pts. wt. chlorinated paraffin, 0.3-0.6 pt. wt. selenium yeast, 1-2 pts. wt. oyster shell nanopowder, 1-2 pts. wt. borax, and 2-3 pts. wt. chitosan sugar. The components (except chlorinated paraffin) for soil improving agent are ground, stirred and granulated for 20-30 degrees C. The granulated particles are added to a roll package clothing pot and maintained at 45-50 degrees C. Molten chlorinated paraffin is sprayed on the surface of the particles to form a uniform coating, and dried at room temperature to obtain the soil improving agent. An INDEPENDENT CLAIM is included for preparation of coated fertilizer.
NOVELTY - Fertilizer for tomato plant comprises 0.5-1 pts. wt. dipterex, 0.2-1 pts. wt. monocrotophos, 35-40 pts. wt. urea, 25-30 pts. wt. calcium biphosphate, 18-25 pts. wt. potassium sulfate, 3-8 pts. wt. zinc sulfate, 0.5-2 pts. wt. borax, 0.5-1 pts. wt. ammonium molybdate, 10-15 pts. wt. horse dung, 5-10 pts. wt. chicken manure, 15-22 pts. wt. canal mud, 8-15 pts. wt. plant ash, 30-35 pts. wt. peat, 15-22 pts. wt. human and animal waste, and 1-3 pts. wt. ectomycorrhizal fungi.    USE - As fertilizer for tomato plant.    ADVANTAGE - The fertilizer has increased durability, improves soil fertility, is cost-effective and improves yield of plant.
NOVELTY - Tobacco-specific ecological carbon base fertilizer comprises 60-120 pts. wt. tobacco stem, 15-30 pts. wt. tobacco waste, 5-10 pts. wt. tobacco waste capable of converting into biocharcoal and wood vinegar, 6-12 pts. wt. chinaberry seed, 6-15 pts. wt. Artemisia annua, 5-14 pts. wt. decanted grass powder, 4-12 pts. wt. Euphorbia lunulata powder, and 50-120 pts. wt. fermented plant organic matter powder.    USE - As tobacco-specific ecological carbon base fertilizer.    ADVANTAGE - The fertilizer improves soil ecosystem, soil water retention ability and fertility, replenish soil nutrients, prevents disease and pest of tobacco, improves quality and yield of tobacco plant, and is environmentally friendly.
NOVELTY - Acidic ionic liquid and solvent are added to reactant comprising chitin or chitosan, mixed, reacted at 500 degrees C or less for 0.01-100 hours, and reaction solution is extracted to obtain levulinic acid. The acidic ionic liquid is recycled after use. The mass ratio of acidic ionic liquid and reactant is 10000 or less. The mass ratio of solvent and reactant is 10000 or less.    USE - Direct conversion of chitin or chitosan to levulinic acid (claimed).    ADVANTAGE - The method provides levulinic acid with yield of 80%, by economical and environmentally-friendly process. The device used for producing levulinic acid has excellent corrosion resistance. The acidic ionic liquid is recycled completely and reused.
NOVELTY - The system has a pneuma solid-liquid separating chamber (22) provided with a discharge pipe (20) and a solid-liquid collection inclined face (19). The pneuma solid-liquid separating chamber is fixed with a joint that is connected with a cooling water nozzle (18). The solid-liquid collection inclined face is arranged below a solid-liquid outside discharge pipe (21). A bottom part of a solid-liquid separating chamber (23) is connected with a pump (25) that is fixed with a carbon discharging pipe (26). A carbon base collection inclined surface is formed with a carbon base collection groove.    USE - Rice hull decomposition separating system.    ADVANTAGE - The system heats a rice hull so as to decompose gas, liquid and solid rice husk carbon so as to improve separating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a rice hull decomposition separating system.    Cooling water nozzle (18)    Solid-liquid collection inclined face (19)    Discharge pipe (20)    Solid-liquid outside discharge pipe (21)    Pneuma solid-liquid separating chamber (22)    Solid-liquid separating chamber (23)    Pump (25)    Carbon discharging pipe (26)
NOVELTY - The system has a first-level purifier connected with a second level purifier. An upper wall of a welding plate is connected with an inner filter device. The first-stage purifier is connected with a first cylindrical shell. Inclined angle of a baffle plate is about 1 to 20 degrees. The second level purifier is connected with a second cylindrical shell. An upper end of the first cylindrical shell is opened with a gas inlet. A lower end of the first cylindrical shell is connected with a purification pneumatic outlet. The internal filtering device is formed with absorbing material.    USE - Biomass gasification furnace purification system.    ADVANTAGE - The system is simple in structure, easy to clean, inexpensive, convenient to operate and maintain, and has wide range of applications, better purification effect, large scale popularization and high purification efficiency.    DETAILED DESCRIPTION - The absorbing material is selected from corn core or active carbon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace purification system.
NOVELTY - A composite biodiesel fuel comprises 5-90 wt.% biodiesel oil, 10-95 wt.% methanol or industrial crude methanol, 0.05-10 wt.% emulsifier, 0.01-5 wt.% stabilizer, 0.05-5 wt.% latent solvent, 0.01-5 wt.% combustion improver, 0.01-2 wt.% pour-point depressant, and 0.01-0.5 wt.% nano-additive.    USE - A composite biodiesel fuel (claimed).    ADVANTAGE - The composite biodiesel fuel is efficient and stable, has high burning efficiency or excellent combustion performance, high heat value, and good stability, and is highly safe, clean, and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite biodiesel oil which involves mixing emulsifier, stabilizer, and latent solvent, adding methanol in biodiesel oil, using high-speed cutting dispersion-emulsification machine for 10-30 minutes, adding combustion improver, pour-point depressant, and nano-additive, stirring, and allowing to stand at room temperature.
NOVELTY - A methanol gasoline additive comprises 4-6 pts. wt. xylene, 3-5 pts. wt. propanol, 5-10 pts. wt. methyl tert.-butyl ether, 1-5 pts. wt. isopropanol, 4-9 pts. wt. p-toluidine, 3-8 pts. wt. 2,6-butylated hydroxytoulene, 4-8 pts. wt. dimethoxymethane, 1-5 pts. wt. n-propyl alcohol, 2-6 pts. wt. gasoline, 1-4 pts. wt. petroleum ether, 3-10 pts. wt. polyisobutylene diimide, 3-7 pts. wt. maleic anhydride, 8-15 pts. wt. methyl alcohol, and 5-9 pts. wt. methyl tert.-butyl ether.    USE - A methanol gasoline additive (claimed).    ADVANTAGE - Product has stable performance and reduces harmful substance and environmental pollution.
NOVELTY - A biomass carbon granule comprises 100 pts. wt. lignite, 1-5 pts. wt. straw, 1-5 pts. wt. wood powder, 10-20 pts. wt. slag, 0-5 pts. wt. heavy oil slag, and 0-5 pts. wt. rubber.    USE - A biomass carbon granule (claimed).    ADVANTAGE - Biomass carbon granule is easy to transport and store and has high heat productivity and low sulfur dioxide discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass carbon granule which involves placing straw, wood powder, and slag in crusher, crushing to obtain crushed mixture, adding water, fermenting to obtain alkaline fermented material, adding lignite, heavy oil slag, and rubber powder, mixing, and molding.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for the preparation of biomass carbon granule. (Drawing includes non-English language text).
NOVELTY - Preparation of high content epigallocatechin gallate (EGCG) comprises pre-selecting EGCG-containing tea polyphenol extract, performing dissolution treatment with purified water to get tea polyphenol extract solution; adding ethanol into silica gel, adding into chromatography column; adding tea polyphenol extract solution into chromatography column, adsorbing; eluting with aqueous ethanol; collecting eluate, stopping elution; vacuum-concentrating, adding organic acid, mixing, crystallizing; and rinsing crystals, filtering, and freeze-drying to obtain powdered-shape EGCG.    USE - Method for preparing high content epigallocatechin gallate (claimed).    ADVANTAGE - The environment-friendly, simple and easy method avoids using toxic solvent, uses small solvent, and produces product with good color and luster, high purity and not easy to oxidized. It has good separating effect and short crystallizing time.    DETAILED DESCRIPTION - Preparation of high content epigallocatechin gallate (EGCG) comprises pre-selecting EGCG-containing tea polyphenol extract, performing dissolution treatment with purified water as solvent to obtain tea polyphenol extract solution; adding 1% ethanol into silica gel, mixing uniformly, adding into chromatography column; adding tea polyphenol extract solution into chromatography column, adsorbing tea polyphenol extract solution into silica gel; eluting with 1% aqueous ethanol and 10-20% ethanol by flowing into chromatography column; collecting eluate until 4-6 times the column volume, stopping elution; vacuum-concentrating, adding organic acid, mixing, crystallizing; and rinsing crystals, filtering, and freeze-drying to obtain powdered-shape EGCG.
NOVELTY - An alcohol-based fuel comprises 60-80 pts. wt. methanol, 1-8 pts. wt. ethanol, 0.1-0.5 pt. wt. sodium nitrate, 0.5-3 pts. wt. hydrogen peroxide, 5-15 pts. wt. sodium hydroxide, 0.1-0.5 pt. wt. ferrocene, and 5-16 pts. wt. water.    USE - An alcohol-based fuel (claimed).    ADVANTAGE - The methanol fuel has high heat value, high heat efficiency, low price, high safety, and no residual liquid which causes blackening.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based fuel which involves uniformly mixing 1/5 parts of methanol and ferrocene to obtain agent (A), uniformly mixing water, ethanol, sodium nitrate, hydrogen peroxide, and sodium hydroxide to obtain agent (B), cooling to room temperature, mixing 4/5 parts of methanol and cooled agent (B), adding agent (A), and uniformly stirring.
NOVELTY - Urea is synthesized by taking ammonia and carbon dioxide as raw materials, compressing, low-pressure decomposing, recovering, evaporating urine and granulating.    USE - Method for synthesizing urea (claimed).    ADVANTAGE - The simple method has low cost. The environment-friendly urea has good dissolution.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of a method for synthesizing urea (Drawing includes non-English language text).
NOVELTY - The method involves purifying exhaust gas of a calcium carbide furnace. An adsorption column is filled with regeneration pneuma. Regeneration pneuma heating process is performed to reduce regeneration pneuma dosage. The regeneration pneuma is filled in the calcium carbide furnace. The regeneration pneuma is selected from one of helium, hydrogen, nitrogen, argon, methane, mixed gas, carbon monoxide and carbon dioxide. The adsorption column is contained with 0 to 30wt.% of alumina, 20 to 100wt.% of active carbon and 0 to 80wt.% of silicon glue.    USE - Temperature-changing calcium carbide furnace purification exhaust gas adsorbing method.    ADVANTAGE - The method enables avoiding utilization rate of the regeneration pneuma and reducing production cost with low energy consumption rate and better flexibility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a temperature-changing calcium carbide furnace purification exhaust gas adsorbing method.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has a modifier that generates hydrogen-containing-gas by reforming reaction using the raw material from which the sulfur compound is removed by a desulfurizer (10). A controller (300) outputs signal which stops operation and signals which report that desulfurizer needs to be replaced, when parameter having correlation in accumulation feed rate of component which contributes to electric power generation of raw materials supplied to desulfurizer is more than the predetermined threshold value set based on emitted-heat amount per unit quantity of the raw material.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The modification catalyst of a hydrogen generating apparatus performs poisoning deterioration with a sulfur compound by the breakthrough of the desulfurizer. Thus, the low cost hydrogen generating apparatus is effectively provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Desulfurizer (10)    Combustor (20)    Fuel cell (200)    Controller (300)    Fuel cell system (400)
NOVELTY - N-benzyl-2-(2-nitro-1H-imidazol-1-yl)acetamide is produced which involves reacting N-benzyl-2-hydroxyacetamide and 2-nitro-1H-imidazole.    USE - The method is useful for producing N-benzyl-2-(2-nitro-1H-imidazol-1-yl)acetamide (claimed) used as therapeutic agent which is effective against American trypanosomiasis (Chagas disease) caused by protozoa Tripanosoma cruzi and transmitted by blood-sucking insects of the genera Triatoma or Rhodnius.    ADVANTAGE - The method is a clean, simple, economical, rapid, easily implemented method, does not involve acid or base catalysts in the synthesis process, and is also environment-friendly.    DETAILED DESCRIPTION - N-benzyl-2-(2-nitro-1H-imidazol-1-yl)acetamide of formula (I) is produced which involves reacting N-benzyl-2-hydroxyacetamide of formula (II) and 2-nitro-1H-imidazole of formula (III)..
NOVELTY - A thermal storage material comprises a base material which reversibly changes between an aqueous solution containing a tetraalkylammonium salt and a clathrate hydrate which uses the tetraalkylammonium salt as guest molecules, and sodium tetraborate added to the aqueous solution.    USE - Thermal storage material is used for heat-retention in refrigerators (claimed) used for food preservation, and in iatrotechnique.    ADVANTAGE - The thermal storage material is capable of preventing supercooling, while preventing decrease in thermal storage performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for refrigerator consisting of a refrigeration compartment, and the thermal storage material arranged in the refrigeration compartment.
NOVELTY - Preparation of noble metal nanoparticles comprises mixing Olea Europaea fruit extract and Acacia Nilotica extract for preparing a mixed extract; providing an aqueous solution containing a noble metal compound; and mixing the mixed extract and the aqueous solution.    USE - Method for the preparation of noble metal nanoparticles used for antibacterial and/or cancer treatment including photothermal therapy in treatment of Ehrlich Ascites carcinoma cells (claimed).    ADVANTAGE - The noble metal nanoparticles are environment-friendly, are inexpensive, and are non-toxic. It has abundant natural materials and medical plants.
NOVELTY - This utility new type claims a a biological sewage treatment device, aeration provided with transverse inner nitrifying a filler, middle part of mud-water separating area provided with inner transverse suspension filler, has a pneuma. pipe, a pneuma pipe at the lower part of a filler of a transverse side wall distribution has a opening, a pneuma tube and air branch tube connected, area for water and mud-water separating groove is at the bottom of a channel provided with a sludge reflux pump. This utility new type mud-water separating area is provided with a sludge reflux pump, the inflow groove for water flow to a mud-water separating in area. A water groove for widening, which is good for water inlet and mud-water separating area reflux of mixed liquid fully mixed, increase the bear impact load ability of system. Provided with transverse nitrifying a filler in aeration, greatly increase nitrogen removing efficiency and COD removing efficiency. Using a filler filter chamber to replace the transverse inclined plate depositing pool, the operation is simple, the operation water outlet water quality is good, and the transverse suspension equipped with a use of a filler pipe pneuma and convenient clean.
NOVELTY - The system (100) has a hydrogen capturing domelike element (150) that includes an exterior surface and an interior surface, the domelike element submerged in the body of water, the entire interior surface in contact with the water, and placed above an electrolysis electrodes (135) to capture bubbles of hydrogen (145) that are separated from the water. A storage container (155) is supported by several previously decommissioned maritime resources (105) to hold the hydrogen. A conduit (160) transfers the hydrogen from the hydrogen capturing element to the storage container.    USE - Energy production and distribution system.    ADVANTAGE - An electricity generating apparatus is effectively placed in an off-grid configuration on each of previously decommissioned maritime resources to generate electricity. Electrolysis electrodes are electrically coupled with the electricity generating apparatus and placed to make contact with water in the body of water to perform an electrolysis operation with the water to separate hydrogen from some of the water using the generated electricity from the electricity generating apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of forming an energy producing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production and distribution system.    Distribution system (100)    Maritime resources (105)    Electrolysis electrodes (135)    Hydrogen (145)    Hydrogen capturing domelike element (150)    Storage container (155)    Conduit (160)
NOVELTY - Recovery of natural gas/crude oil involves introducing foam-forming amount of composition comprising homogeneous solution of water insoluble long chain fatty acid and organic solvent into fluid at downhole end of oil well or gas well. The homogeneous solution comprises 30-70 wt.% fatty acid. The fluid comprises hydrocarbon and/or water.    USE - Recovery of natural gas/crude oil (claimed).    ADVANTAGE - The method enables economical recovery of natural gas/crude oil, with high yield.
NOVELTY - Fabrication (100) of catalyst involves contacting (102) substrate containing ceria with solution containing catalytic cations, and contacting (106) the substrate with solution containing promoter cations. The catalytic cations consist of transition metal cations and/or post-transition metal cations. The promoter cations consist of alkali/alkaline earth metal cations.    USE - Fabrication of catalyst used in catalytic converter of automotive vehicle (all claimed).    ADVANTAGE - The catalyst catalyzes reduction of nitric oxide by carbon monoxide or propylene or hydrogen gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst, which comprises substrate including ceria, catalytic cations bound to substrate surfaces, and promoter cations bound to substrate surfaces.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of fabrication of catalyst.    Fabrication process (100)    Contact process (102,106)    Solvent removal process (104,108)    Heating process (110)
NOVELTY - Enhanced production and extra-cellular secretion of lipids comprises (a) obtaining a biomass of an oleaginous microorganism; and (b) culturing the biomass of an oleaginous microorganism in a modified growth medium deficient in nitrogen and iron, resulting in enhanced production and extracellular secretion of lipids.    USE - The method is used for enhanced production and extra-cellular secretion of lipids (claimed).    ADVANTAGE - Provided is a cost-effective and efficient process that eliminates the need for harvesting and rupturing the microbial cells for extraction of the intra-cellular lipids.
NOVELTY - Fermentative production of C4 product from sugar comprises taking lignocellulose-containing biomass, which is obtained from microorganism strain Raoultella terrigena having gene pflB encoding pyruvate formate lyase, then carrying out fermentation in presence of aerobic condition. The sugar xylose and pyruvate formate lyase are not functional, and are enzymatically inactive.    USE - The method is useful for fermentative production of C4 product from sugar (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of microorganism strain Raoultella terrigena with inactive pyruvate formate lyase for fermentative production of C4-product from xylose, which is obtained from lignocellulose-containing biomass.
NOVELTY - The fermenter comprises an inlet (3), an outlet (4) of a tank (2), and a stirrer having a shaft (10) passed through the fermenter in longitudinal direction. The shaft is disposed in multiple stirring arms (12) provided with vanes (13) in ending area (6) of the fermenter.    USE - Fermenter for anaerobic fermentation of biogenic waste for producing energy in gaseous form for generating electrical energy for small facilities.    ADVANTAGE - The fermenter shows simple structure with enhanced working efficiency, and degrades the biogenic residue by using controlled mixing, and thus significantly reduces environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the fermenter.    Tank (2)    Inlet (3)    Outlet (4)    Ending area (6)    Shaft (10)    Stirring arms (12)    Vanes (13)
NOVELTY - The apparatus (200) has control unit that applies a voltage between the anode (208) and the cathode (210), and the electrical potential difference between the anode and the cathode maintain a constant current until reaching a predetermined upper limit electrical potential difference. The oxygen reduction control applies a constant voltage between the anode and the cathode so that the upper limit electrical potential difference may not be exceeded will be performed, when the electrical potential difference attains the upper limit electrical potential difference.    USE - Oxygen reduction apparatus for refrigerator (claimed).    ADVANTAGE - Since the oxygen reduction control applies a constant voltage between the anode and the cathode so that the upper limit electrical potential difference may not be exceeded will be performed, when the electrical potential difference attains the upper limit electrical potential difference, the oxygen reduction apparatus can keep hydrogen from generating.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the refrigerator. (Drawing includes non-English language text).    Container accommodating portion (104)    Reduction container (106)    Oxygen reduction apparatus (200)    Anode (208)    Cathode (210)
NOVELTY - Preparing soil conditioner involves inoculating microbial species such as Bacillus subtilis, Bacillus pumilus, and Saccharomyces cerevisiae into seed culture media, and then performing incubation at certain temperature for 3-5 days to obtain seed broth.    USE - Method for preparing soil conditioner (claimed).    ADVANTAGE - The method enables to prepare soil conditioner by utilizing molasses resource in a cost-effective manner.    DETAILED DESCRIPTION - Preparing soil conditioner involves inoculating microbial species such as Bacillus subtilis, Bacillus pumilus, and Saccharomyces cerevisiae into seed culture media, and then performing incubation at certain temperature for 3-5 days to obtain seed broth. The certain amount of inoculum taken out from the seed broth, substrate, and alcoholic wastewater containing inorganic matter i.e. 0.84-1.98 g/kg phosphorus, 35.12-90.93 g/kg potassium, 5.55-39.90 g/kg calcium, 1.02-70.31 g/kg magnesium, and 16.52-50.40 g/kg nitrogen, are then added into the fementer to perform fermentation at certain temperature 5-7 days. The obtained fermentation broth is then concentrated to obtain soil conditioner as the finished product.
NOVELTY - Ensfer meliloti strain, resistant to Sophora flavescens matrine, is new. The strain has preservation number of CGMCC No.9296.    USE - The strain is useful for reducing Rhizobium contamination rate and increasing nodule occupancy rate (claimed).    ADVANTAGE - The strain is environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) use of the strain for reducing Rhizobium contamination rate and increasing nodule occupancy rate; (2) producing anti-contaminating Rhizobium, comprising fermentation culturing Ensfer meliloti strain in a broth and mixing with matrine antibacterial liquid; and (3) anti-contaminating rhizobium.
NOVELTY - Chitinase producing strain comprising Paenibacillus pasadenensis CS0611 preserved in China Center for Type Culture Collection with preservation serial number of CCTCC N0: M2014458 on October 8, 2014, is new.    USE - The strain is useful for producing chitinase by crab shells fermentation (claimed).    ADVANTAGE - The fermentation method: is simple; has low cost; achieves fermentation broth activity up to 211.3 mu m/ml; can hydrolyze shrimp crab shells waste; and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the strain useful for producing chitinase by crab shells fermentation, comprising inoculating the strain into fermentation culture medium, where initial pH of the fermentation culture medium is 5-8.5, fermenting at 28-40 degrees C for 48-96 hours, centrifuging to remove the strain cells and crab shell powder, and taking fermentation supernatant, i.e., chitin crude enzyme solution b, where the fermentation culture medium comprises 0.5-20 g/l crab shell powder, 0.5-1 g/l dipotassium hydrogen phosphate, 0.2-0.5 g/l potassium dihydrogen phosphate, 0.3-0.7 g/l magnesium sulfate, and 0.8-1.2 g/l sodium chloride.
NOVELTY - A rice composite fertilizer comprises 5-10 pts. wt. urea, 5-10 pts. wt. sulfuric acid, 4-6 pts. wt. malonic acid, 1-2 pts. wt. phosphonium acid, 1-2 pts. wt. ammonium chloride, 0.1-2 pts. wt. nitrogen bacteria fertilizer, 0.1-2 pts. wt. phosphonium bacteria fertilizer and 0.2-0.4 pt. wt. micronutrient fertilizer.    USE - Rice composite fertilizer.    ADVANTAGE - The fertilizer has 6% increase product yield per unit area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite fertilizer comprising taking raw materials, stirring, adding 2 times kaolin, and granulating.
NOVELTY - The method involves using raw water oligotrophic environment microorganisms. The biological film is formed on different carriers in different reaction chambers of the grid. The different cultivating microorganism is planted and cultivated. The nitrogen and organic matter in the raw water are removed. The raw water is measured under different habitats.    USE - Raw water biological pre-processing method.    ADVANTAGE - The aeration effect of the raw water is improved. The energy consumption of the high aeration condition operation is reduced. The flexibility of process operation is improved. The operation process is simple, the operation is convenient and capital construction cost is reduced.
NOVELTY - Microbial fertilizer comprises 0.5-5 pts. wt. Bacillus subtilis, 0.3-4 pts. wt. Bacillus megaterium, 0.5-3 pts. wt. silicate bacteria, 0.2-3 pts. wt. Streptomyces, 0.3-5 pts. wt. Pseudomonas, 0.1-3 pts. wt. Escherichia coli, 0.2-5 pts. wt. additive and 72-97.2 pts. wt. water-soluble organic carrier. Additive is brown sugar, sucrose or molasses. Organic carrier is humic acid, fulvic acid, composite amino acid, activated carbon, peat, decomposed bacterial residue, plant polysaccharide, decomposed organic material and/or plant protein.    USE - Microbial fertilizer used for increasing crop resistance and improving crop yield.    ADVANTAGE - The fertilizer has reduced production cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of microbial fertilizer comprising taking raw materials, mixing and soaking in culture medium for 12-48 hours; and    (2) application of microbial fertilizer comprising taking fertilizer, spraying and performing irrigation.
NOVELTY - An organic fertilizer comprises 30-80 pts. wt. chicken manure, 20-50 pts. wt. straw, 5-15 pts. wt. coal gangue, 10-30 pts. wt. pond sludge, 5-15 pts. wt. peat moss, 5-30 pts. wt. rock phosphate, 1-30 pts. wt. potassium ore, 5-30 pts. wt. vermicompost, 5-25 pts. wt. tea residue, 10-20 pts. wt. oil cake, 5-25 pts. wt. rice husk powder, 1-5 pts. wt. bacteria powder, and 1-15 pts. wt. urea.    USE - Organic fertilizer is used for leafy vegetable.    ADVANTAGE - The organic fertilizer has fast fermentation rate, short fermentation time, high organic matter, high humus, rich in nutrients, and rapid fertilizer effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of organic fertilizer.
NOVELTY - A mulberry planting fertilizer comprises 80-100 pts. wt. chicken manure, 30-50 pts. wt. humic acid, 60-80 pts. wt. dry biogas, 20-30 pts. wt. weathered coal, 1-3 pts. wt. boron fertilizer, 3-5 pts. wt. ferrous sulfate, 5-10 pts. wt. ammonium molybdate, 50-70 pts. wt. canal mud, 10-15 pts. wt. EM microbial inoculum and 80-100 pts. wt. straw.    USE - Mulberry planting fertilizer is used for soil.    ADVANTAGE - The reliable, nutritional and efficient mulberry planting fertilizer has excellent conductivity to absorption of mulberry, and prevents soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mulberry planting fertilizer.
NOVELTY - A watermelon rind-containing fertilizer comprises Phyllostachys edulis, bean dregs, animal offal, plant ash, biscuit crumbs, chicken feces, humic acid, peanut cake, pig manure, ceramsite, pine pollen, Indus flower, tobacco, safflower, Angelica powder, watermelon rind, bone, spoiled sweet potato, white clay and Curculigo.    USE - Watermelon rind-containing fertilizer is used for rapeseed.    DETAILED DESCRIPTION - A watermelon rind-containing fertilizer comprises 15-20 pts. wt. Phyllostachys edulis, 10-13 pts. wt. bean dregs, 20-40 pts. wt. animal offal, 1-2 pts. wt. plant ash, 1-2 pts. wt. biscuit crumbs, 55-65 pts. wt. chicken feces, 1-2 pts. wt. humic acid, 1-2 pts. wt. peanut cake, 20-30 pts. wt. pig manure, 1-3 pts. wt. ceramsite, 3-6 pts. wt. pine pollen, 1-2 pts. wt. indus flower, 0.2-0.3 pts. wt. tobacco, 2-4 pts. wt. safflower, 1-3 pts. wt. Angelica powder, 4-6 pts. wt. watermelon rind, 2-4 pts. wt. bone, 4-7 pts. wt. spoiled sweet potato, 1-2 pts. wt. white clay and 1-2 pts. wt. Curculigo.
NOVELTY - Recovering triphenylmethanol from olmesartan medoxomil wastewater comprises adding activated carbon to olmesartan medoxomil production waste liquid, decoloring, filtering, processing filtrate under reduced pressure to recover solvent, adding diluted acid, crystallizing, centrifuging to obtain crude triphenylmethanol; and recrystallizing with solvent.    USE - Method for recovering triphenylmethanol from olmesartan medoxomil wastewater (claimed).    ADVANTAGE - The method is easy to control, stable and environment-friendly, and has low cost, and high recovery rate.
NOVELTY - A 2,4-dichlorophenoxyacetic acid is prepared by taking chloroacetic acid and sodium hydroxide solution, stirring for 15-20 minutes, adding phenol, regulating pH to 11 by adding sodium bicarbonate, heating at 100 degrees C for 40 minutes, adding hydrochloric acid, adjusting pH to 4, cooling, drying, adding acetic acid and water solution, mixing, adding 0.1 wt.% iron phthalocyanine, stirring, introducing chlorine, carrying out chlorination reaction for 35-50 minutes, cooling, filtering, drying.    USE - Method for preparing 2,4-dichlorophenoxyacetic acid (claimed).    ADVANTAGE - The method is simple, low-cost and environment-friendly. It has high product yield and purity.
NOVELTY - Extraction of taurine comprises carrying out preliminary purification of mother liquor containing taurine and inorganic salts, collecting liquid taurine with concentration of greater than or equal to 99.0%, feeding the remaining primary liquid taurine and inorganic salt solution into the purification section, collecting, purifying primary taurine solution through online monitoring, collecting, repurifying the rest of liquid taurine and inorganic salt solution, collecting, separating, incorporating the separated taurine solution with purified liquid taurine through online monitoring and collecting.    USE - Method for extracting taurine (claimed).    ADVANTAGE - The method is environment-friendly and has reduced energy consumption and high yield.    DETAILED DESCRIPTION - Extraction of taurine comprises carrying out preliminary purification of mother liquor containing taurine and inorganic salts, collecting liquid taurine with concentration of greater than or equal to 99.0%, feeding the remaining primary liquid taurine and inorganic salt solution into the purification section, collecting, purifying primary taurine solution through online monitoring to concentration of higher than 99.0%, collecting, repurifying the rest of liquid taurine and inorganic salt solution, collecting, separating, incorporating the separated taurine solution with purified liquid taurine through online monitoring and collecting. An INDEPENDENT CLAIM is included for taurine purification device comprising taurine liquor collecting barrel, primary high pressure pump, primary column, primary liquid chromatography column, front transit barrels, high-pressure pump, front column, liquid phase chromatograph, transit barrels, high pressure pump, chromatography column, liquid phase chromatograph column, taurine collection valve, taurine collection barrel, inorganic salt collection valve, inorganic salt collection barrels, water collection valve and water collection barrel.
NOVELTY - Preparation of manidipine hydrochloride comprises adding crude manidipine hydrochloride to a mixed solvent of acetone and water, dissolving by heating, and adding activated carbon to the solution, incubating, stirring, filtering, crystallizing, filtering, collecting precipitated solid, and drying under vacuum to give a solid crystalline form of manidipine hydrochloride.    USE - Method for preparing manidipine hydrochloride (claimed).    ADVANTAGE - The method is simple and environment-friendly, has high yield, is suitable for large scale production, and can prepare manidipine hydrochloride having high purity.
NOVELTY - 2,4,6-Trichloropyrimidine(I) and 4-hydroxy-3,5-dimethylbenzonitrile (II) are reacted, to obtain 4-((2,6-dichloropyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile (III). Compound (III) and cyanoaniline are reacted, to obtain 4-((6-chloro-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile (IV). Compound (IV) is ammoniated, to obtain 4-((6-amino-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile (V). Compound (V) is brominated, to obtain 4-((6-amino-5-bromo-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile (VI).    USE - Synthesis of 4-((6-amino-5-bromo-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile (claimed).    ADVANTAGE - The method enables preparation of 4-((6-amino-5-bromo-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile with high productivity by simple process in a short period of time with reduced energy consumption.    DETAILED DESCRIPTION - 2,4,6-Trichloropyrimidine of formula (I) and 4-hydroxy-3,5-dimethylbenzonitrile of formula (II) are reacted in presence of base, to obtain 4-((2,6-dichloropyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile of formula (III). Compound (III) and cyanoaniline are reacted in presence of alkaline compound, to obtain 4-((6-chloro-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile of formula (IV). Compound (IV) is ammoniated in microwave reactor, to obtain 4-((6-amino-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile of formula (V). Compound (V) is brominated, to obtain 4-((6-amino-5-bromo-2-((4-cyanophenyl)amino)pyrimidin-4-yl)oxy)-3,5-dimethylbenzonitrile of formula (VI).
NOVELTY - Applying pesticide on soybean involves spraying of pesticide on leaf. Pesticide comprises liquid mixture A, B and C. Liquid mixture A comprises 25 wt.% abamectin aqueous dispersion 3-5g, 20 wt.% Bordeaux mixture 15-18g, ammonium citrate 90-100g, 25 wt.% triazolone 12-18g, 95 wt.% 4-chloroindole-3-acetic acid 3-5g and water 40-50kg. Liquid mixture B comprises 30 wt.% abamectin aqueous dispersion 4-8g, 48 wt.% tebuconazole aqueous dispersion 18-22g, 20 wt.% Bordeaux mixture 10-12g, 98 wt.% ammonium citrate 4-6g, 21 wt.% boric acid 12-15g and water 50-55kg.    USE - Method for applying pesticide on soybean (claimed).    ADVANTAGE - The method is eco-friendly, and enables to reduce pesticide dosage on crop.    DETAILED DESCRIPTION - Applying pesticide on soybean involves spraying of pesticide on leaf. Pesticide comprises liquid mixture A, B and C. Liquid mixture A comprises 25 wt.% abamectin aqueous dispersion 3-5g, 20 wt.% Bordeaux mixture 15-18g, ammonium citrate 90-100g, 25 wt.% triazolone 12-18g, 95 wt.% 4-chloroindole-3-acetic acid 3-5g and water 40-50kg. Liquid mixture B comprises 30 wt.% abamectin aqueous dispersion 4-8g, 48 wt.% tebuconazole aqueous dispersion 18-22g, 20 wt.% Bordeaux mixture 10-12g, 98 wt.% ammonium citrate 4-6g, 21 wt.% boric acid 12-15g and water 50-55kg. Liquid mixture C comprises 50 wt.% tebuconazole aqueous dispersion 30-40g, naphthalene acetic acid 15-20g, potassium dihydrogen phosphate 50-60g and water 40-50kg.
NOVELTY - Preparing eco-friendly pesticide involves drying camphor tree leaves and crushing through 50 meshes to obtain powder. 35 pts. Industrial alcohol (90%) is mixed with powder in water bath and then refluxing for 1.5 hours to obtain liquid. Liquid is filtered to obtain filter liquor and residue. Residue is refluxed with 15 parts industrial alcohol (80%) for 10 hours and then filtered to obtain another filter liquor. Filter liquors are combined at 4 degrees C and then water is mixed in ratio of 1:2 and frozen at -30 degrees C. The freeze dried product is concentrated to obtain concentrated powder.    USE - Method for preparing eco-friendly pesticide (claimed).    ADVANTAGE - The method enables to prepare eco-friendly pesticide is easy to decompose and tasteless, and ensures no toxic and side effects to soil.    DETAILED DESCRIPTION - Preparing eco-friendly pesticide involves drying camphor tree leaves and crushing through 50 meshes to obtain powder. 35 pts. Industrial alcohol (90%) is mixed with powder in water bath and then refluxing for 1.5 hours to obtain liquid. Liquid is filtered to obtain filter liquor and residue. Residue is refluxed with 15 parts industrial alcohol (80%) for 10 hours and then filtered to obtain another filter liquor. Filter liquors are combined at 4 degrees C and then water is mixed in ratio of 1:2 and frozen at -30 degrees C. The freeze dried product is concentrated to obtain concentrated powder, and then modified starch and licorice powder are added in ratio of 8:1:3 to obtain a product. 45 wt.% The product is mixed with 15 wt.% tomato pigment, 10 wt.% allethrin, 15 wt.% clove oil and 15 wt.% gossypol.
NOVELTY - A carbon gel catalyst comprises carbon material having whole solid block of any shape, and fixed bed catalyst. The carbon material is a graphite oxide, porous graphene oxide, carboxylated carbon tube and/or its modified product.    USE - Carbon gel catalyst used in complex organic reaction catalysis field (claimed).    ADVANTAGE - The catalyst exhibits fast and efficient catalytic effects, has simple process, and has high yield and high selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of the catalyst which comprises putting 5-300 mg/mL carbon material solution to a reactor, putting in freezing dryer, and spray drying.
NOVELTY - A Ginkgo leaf mushroom mycelium is produced by: collecting Ginkgo leaf, and drying; weighing Ginkgo leaf, sawdust, wheat bran, urea, white granulated sugar, calcium superphosphate and gypsum; crushing Ginkgo leaf, adding sawdust and Aspergillus niger, and biodegrading; adding wheat bran, urea, white granulated sugar, calcium superphosphate and gypsum, and regulating water content and pH; packing, and sterilizing; cooling, covering film, and standing; controlling temperature, piercing hole, and piling into triangle; and harvesting.    USE - Method for producing Ginkgo leaf mushroom mycelium (claimed).    ADVANTAGE - The method shortens mycelium culture time, increases production efficiency, reduces production cost, increases industrial and agricultural waste use, and protects environment.    DETAILED DESCRIPTION - A Ginkgo leaf mushroom mycelium is produced by: collecting Ginkgo leaf, and drying; weighing Ginkgo leaf, sawdust, wheat bran, urea, white granulated sugar, calcium superphosphate and gypsum; crushing Ginkgo leaf into 0.3-0.5 cm, adding sawdust and Aspergillus niger, and biodegrading; adding wheat bran, urea, white granulated sugar, calcium superphosphate and gypsum, regulating water content to 50-60% and pH to 5.5-6, and stir mixing to prepare cultivation matrix material; packing, and sterilizing for 4 hours; cooling, placing into room, covering film, and standing; controlling temperature at 24-27 degrees C after 7-15 days, piercing hole at 15-20 at 35-45, holding temperature at 25-28 degrees C, and piling into triangle with height of not greater than 10 layers; and harvesting.
NOVELTY - Preparing organic composite fertilizer involves mixing municipal sludge containing water content 75-85% with de-watered sludge with water content less than 15% in volume ratio of 1:1-2, and then dehydrated to obtain dry sludge. Composting of dry sludge is carried out, where mixture material with water 50-65% is settled in bottom of a fermentation pool. Top part is set with plate of the fermentation pool. Fermentation of dry sludge is carried out two times in the fermenting pool by utilizing biological microbial inoculum.    USE - Method for preparing organic composite fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic composite fertilizer, which is easy to absorb by soil.    DETAILED DESCRIPTION - Preparing organic composite fertilizer involves mixing municipal sludge containing water content 75-85% with de-watered sludge with water content less than 15% in volume ratio of 1:1-2, and then dehydrated to obtain dry sludge. Composting of dry sludge is carried out, where mixture material with water 50-65% is settled in bottom of a fermentation pool. Top part is set with plate of the fermentation pool. Fermentation of dry sludge is carried out two times in the fermenting pool by utilizing biological microbial inoculum 1000 billion/g matrix i.e. Azotobacter, phosphorus solubilizing microorganism, potassium solubilizing bacteria or their mixture at 48-55 degrees C for 3-8 days and then 50 degrees C for 2 weeks with ventilation of 6-12 m3/m3 material/hour and 8-15 m3/m3 material/hour respectively. The fermented product is dried and crushed to obtain product with water less than 10%. Rotten of matrix is mixed with the product with water less than 10% in weight ratio of 1:50-100, and then dried at 60 degrees C to obtain fertilizer with water content 5-10%. The fertilizer is cooled and packaged to obtain the product.
NOVELTY - Preparing organic fertilizer involves primary dehydrating of sludge through squeezing and dehydrating devices, which reduces sludge water to 50-60%. Dehydrated sludge is mixed with straw and chicken manure according to their respective ratio into a reaction kettle by using steam under certain temperature, pressure, catalyst and additive for 1.5 hours. Insect eggs, toxic pathogen substance, macromolecular organic substance i.e. carbohydrate and humic acid of small plant are added in the kettle. Nitrogen, phosphorus and potassium is mixed with obtained product, granulated it, and then dried.    USE - Method for preparing organic fertilizer (claimed) used for improvement of soil.    ADVANTAGE - The method enables to prepare water-retaining and drought resistant organic fertilizer in simple, eco-friendly and cost-effective manner within short period.    DETAILED DESCRIPTION - Preparing organic fertilizer involves primary dehydrating of sludge through squeezing and dehydrating devices, which reduces sludge water to 50-60%. Dehydrated sludge is mixed with straw and chicken manure according to their respective ratio into a reaction kettle by using steam under certain temperature, pressure, catalyst and additive for 1.5 hours. Insect eggs, toxic pathogen substance, macromolecular organic substance i.e. carbohydrate and humic acid of small plant are added in the kettle. Nitrogen, phosphorus and potassium is mixed with obtained product, granulated it, and then dried and cooled.
NOVELTY - The system has a semi-permeable membrane (118) as anion exchange membrane is placed between anaerobic digestion chamber and aerobic nitrification reactor (116) having substances, allowing first substance to pass between chambers while prohibiting passage of second substance. A mechanical filter is fluidically connected between anaerobic digestion chamber and aerobic nitrification reactor for separating materials suitable for treatment in anaerobic digestion chamber not in aerobic nitrification reactor from material to be treated in aerobic nitrification reactor.    USE - System for treating multi-component waste streams of water from residential, commercial, municipal, industrial or agricultural sources.    ADVANTAGE - The multi-component waste streams can be treated with economical reduction of ammonia concentrations to the development of more stable, cost-effective anaerobic digester and enabling the combined reduction or removal of total solids (TS), chemical oxygen demand (COD), and nitrogen. The aerobic conditions in the second chamber from interfering with the anaerobic character of the first chamber are prevented. The reduction to biogas end products such as carbon dioxide and potentially methane and/or hydrogen can be prevented, by balancing the rate of COD solubilization and the nitrate delivery rate into the digestate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating waste stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the packaged configuration of the components.    Aerobic nitrification reactor (116)    Semi permeable membrane (118)    Compounds (128)
NOVELTY - Biogas purification system comprises contaminant-removal module containing catalytic oxidation catalyst comprising vanadium oxide provided on a metal oxide support, contaminant-removal module containing alkali-impregnated carbon, in which the 5-15 wt.% alkali comprises an ionic salt of an alkali metal or alkaline earth metal. The contaminant-removal module removes 85% or more of acidic reaction products. The catalyst oxidizes 85% or more of sulfur and halogenated compounds.    USE - Biogas purification system is used for removing sulfur and halogenated compounds, and acidic reaction product from biogas (all claimed).    ADVANTAGE - The biogas purification system enables efficient purification of biogas by economical and environmentally-friendly process. The purified biogas provided by the method has excellent quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of removing sulfur and halogenated compounds, and acidic reaction product from biogas.
NOVELTY - Town waste solid-liquid separated fermentation treatment pool comprises a pool body (1), where the pool body is provided with V-shaped baffle plate constituting solid state fermentation chamber and liquid fermentation room. The top part of pool body is set with reverse V-shaped roof (2). The upper end of pool body is equipped with a dustbin (3). The V-shaped baffle plate and pool body four surfaces are fixed. The V-shaped baffle plate is equipped with a pull sliding long stick.    USE - Used as town waste solid-liquid separated fermentation treatment pool.    ADVANTAGE - The pool prevents generation of harmful substance, has simple structure, requires less space, does not pollute environment, and has wide popularization and application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the town waste solid-liquid separated fermentation treatment pool.    Pool body (1)    Reverse V-shaped roof (2)    Dustbin (3)    Waste gas and liquid through pipe (4)    Waste gas and liquid hole (5)
NOVELTY - Biofertilizer comprises 20-25% calcium superphosphate, 18-24% complex amino acid powder, 0.04-0.08% Bacillus subtilis and 52.93-60.97% pre-processed poultry excrement.    USE - The biofertilizer is useful in aquaculture.    ADVANTAGE - The fertilizer: has no side effects and free of toxins; is capable of cultivating fish; and improves water quality and feed conversion rate.
NOVELTY - A wastewater treating method involves adding straw powder, white rot fungus spore suspension, and trace element liquid containing methylene blue to obtain mixed liquid, followed by spraying mixed solution at 25-40 degrees C for treating wastewater.    USE - Method for treating wastewater.    ADVANTAGE - The method enables treating wastewater with high efficiency and good effect in a simple, cost effective and eco-friendly manner.
NOVELTY - Cultivation substrate comprises 30-60 pts. wt. crushed garlic straw, 30-60 pts. wt. cotton seed hull, 10-20 pts. wt. wheat bran, 1-3 pts. wt. quicklime, 1-2 pts. wt. stone bone, 0.5-1 pts. wt. urea and 0.5-1 pts. wt. phosphoric acid.    USE - Cultivation substrate used for cultivating oyster mushroom (claimed).    ADVANTAGE - The cultivation substrate is cost-effective and eco-friendly, and is required in low amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing cultivation substrate, which involves:    (A) drying and crushing mildew free garlic straw to obtain garlic straw powder;    (B) mixing garlic straw powder with cotton seed hulls and wheat bran to obtain mixture;    (C) mixing quicklime, gypsum, urea, stone bone and water to obtain liquid mixture;    (D) mixing liquid mixture with obtained wheat bran mixture;    (E) fermenting obtained mixture for 5-18 days at 60 degrees C;    (F) cooling fermented mixture to obtain cultivation matrix;    (G) packing obtained product in polyethylene rubber bag; and    (H) storing product at controlled temperature and humidity for specified period of time.
NOVELTY - A 4-phenyl- alpha -aminobutyric acid is prepared by reacting phenylpropionaldehyde, L-benzene ammonia alcohol, and trimethyl cyanide (TMSCN) in solvent in presence of catalyst A at 0-70 degrees C for 1-8 hours, purifying to obtain compound, adding obtained compound and acid in solvent, heating at 50-120 degrees C, refluxing for 3-10 hours, carrying out hydrolysis reaction, finishing reaction with alkali solution, adjusting pH to 4-5, purifying to obtain compound, dissolving obtained compound in organic solvent, adding catalyst B, and introducing hydrogen.    USE - Preparation of 4-phenyl- alpha -aminobutyric acid (claimed).    ADVANTAGE - Method is simple, costs low and is environmentally friendly.    DETAILED DESCRIPTION - A 4-phenyl- alpha -aminobutyric acid of formula (V) is prepared by reacting phenylpropionaldehyde of formula (I), L-benzene ammonia alcohol of formula (II), and trimethyl cyanide (TMSCN) in solvent in presence of catalyst A at 0-70 degrees C for 1-8 hours, purifying to obtain compound (III), adding compound (III) and acid in solvent, heating at 50-120 degrees C, refluxing for 3-10 hours, carrying out hydrolysis reaction, finishing reaction with alkali solution, adjusting pH to 4-5, purifying to obtain compound (IV), dissolving compound (IV) in organic solvent, adding catalyst B, introducing hydrogen, and stirring at normal pressure for 4-12 hours at 20-60 degrees C under hydrogenation reduction reaction. Catalyst A is magnesium iodide, magnesium bromide, magnesium chloride, magnesium perchlorate or trifluoromethane sulfonic acid magnesium. Acid is hydrochloric acid, hydrobromic acid, hydroiodic acid, sulfuric acid, nitric acid, perchloric acid or acetic acid. Catalyst B is palladium, palladium carbon or Raney nickel. Organic solvent is methyl alcohol, ethyl alcohol, isopropyl alcohol, ethyl acetate, acetic acid, acetic acid propyl acetate, butyl acetate, tetrahydrofuran, or methyl tetrahydrofuran.
NOVELTY - Lignocellulosic biomass is processed with mixed solvent of water and alkylene glycol, heat-extracted and solid-liquid separation is carried out, such that liquid component containing lignin and solid component containing cellulose are separated.    USE - Separation of lignin component and cellulose component used in manufacture of thermoplastic lignin composite and saccharification material (all claimed) for chemical substance, pharmaceutical, agrochemical, fragrance and food additive. The saccharification material is useful for manufacture of biomass fuels e.g. bioethanol, and functional biomass materials.    ADVANTAGE - The lignin component is extracted with high yield by simple process. Saccharification material and thermoplastic lignin component are manufactured with high quality from lignin component by simple and economical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of thermoplastic lignin composite, which involves distilling mixed solvent of water and alkylene glycol from the liquid component containing lignin; and    (2) manufacture of saccharification material, which involves removing solid component containing cellulose using solid-liquid separation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining separation method of lignin component and cellulose component, and the manufacturing method of thermoplastic lignin composite and saccharification material. (Drawing includes non-English language text)
NOVELTY - Recovering oil in a corn to ethanol process where oil and solids are present in a process stream mixture, comprises adding an oil separation aid to the process stream mixture. The oil separation aid comprises: a non-ionic surfactant comprising a polyol derived from a sorbitol, a sorbitan, or isosorbide; and an ester of a polyethylene glycol and a fatty acid.    USE - The method is useful for recovering oil in a corn to ethanol process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a corn oil separation enhancement composition comprising an alkoxylated sorbitan alkylate and a polyethylene glycol ester of a fatty acid.
NOVELTY - This utility new type claims a rural sewage treatment and a fermentation device, comprising a drain outlet, and dismounting mechanism, a hoop, pressure table, automatic exhaust valve, sense hole, a pressure material rod, sewage and waste material adding device, a filtering device and inflow floating ball switch, a drain wherein b hair. l... screen periphery of hair b l, the pressing material plate, and wall and inner hair l tightly contact, the hoop and detachable clamping connection mechanism, a pressure table and pressure material rod top end connection, the automatic exhaust valve set pressure table, the b and pressure material rod and connected, this sewage treatment and fermentation device, a domestic sewage or livestock waste foot material collective to carry out fermenting, then get again using a can on the ground fertilizer, so the waste is valuable, environment-friendly and energy-saving, with centrifuge motor a waste in a whole inner fully mixed, a rate increase.
NOVELTY - Glycyrrhizic acid derivatives are hydrolyzed by dissolving glycyrrhizic extract acid in organic solvent, adjusting pH value to 1-3, pumping into subcritical reactor using high pressure infusion pump, hydrolyzing using subcritical water, stirring, reacting, collecting reacted solution, centrifuging, extracting with organic solvent to obtain aqueous phase and organic phase, concentrating aqueous phase to soluble solid content of 25-40%, removing organic solvent phase, reconstituting with absolute ethanol, and drying.    USE - Method for hydrolyzing glycyrrhizic acid derivatives (claimed) used as food additives and pharmaceutical precursors.    ADVANTAGE - The method is environment-friendly, and has high product yield.
NOVELTY - Preparation of nitrobenzyl alcohol involves dissolving nitrotoluene as raw material in carbon tetrachloride solvent, adding benzoyl peroxide catalyst, stirring at 150-180 degrees C for 1-2 hours, reacting for 1-5 hours, obtaining nitrobenzyl chloride, crystallizing, purifying, obtaining purified nitrobenzyl chloride crystals, hydrolyzing in alkaline solution and distilling. The chlorine gas discharged during the reaction process is continuously subjected to chromatographic analysis to control of nitrobenzyl chloride initial yield to 20-66%.    USE - Preparation of nitrobenzyl alcohol (claimed).    ADVANTAGE - The method efficiently provides nitrobenzyl alcohol by simple, environmentally-friendly and economical process in short period of time.    DETAILED DESCRIPTION - Preparation of nitrobenzyl alcohol involves dissolving nitrotoluene as raw material in carbon tetrachloride solvent, adding benzoyl peroxide catalyst, stirring at 150-180 degrees C for 1-2 hours, reacting for 1-5 hours, obtaining nitrobenzyl chloride, crystallizing, purifying, obtaining purified nitrobenzyl chloride crystals, hydrolyzing in alkaline solution and distilling. The chlorine gas discharged during the reaction process is continuously subjected to chromatographic analysis to control of nitrobenzyl chloride initial yield to 20-66%. The raw material is distilled under steam to improve overall yield of nitrobenzyl chloride.
NOVELTY - A water retaining sustained release light soil nutrient comprises 10-30 wt.% peat soil, 5-15 wt.% bone meal, cinder ash, 5-15 wt.% desulfurized gypsum powder composition, 10-40 wt.% functional matrix, 10-30 wt.% decomposed manure, 0-10 wt.% oil cypress, 1-10 wt.% microbial fertilizer, 10-30 wt.% inorganic adsorbent, 10-30 wt.% inorganic mineral powder, 5-10 wt.% germicidal pesticide, 1-10 wt.% beneficial microorganisms composition powder and 0-10 wt.% pH regulators.    USE - Water retaining sustained release light soil nutrient used for organic farming and green roof applications.    ADVANTAGE - The water retaining sustained release light soil nutrient is prepared economically using readily available raw materials, has excellent durability, water retention property, sustained fertility, and ecological self-circulation property.
NOVELTY - Fertilizer comprises 300-500 pts. wt. plant ash, 100-200 pts. wt. peanut, 600-1000 pts. wt. fermented livestock manure, 10-20 pts. wt. potassium nitrate, 3-5 pts. wt. borax, 8-15 pts. wt. manganese sulfate, 6-10 pts. wt. zinc sulfate and 300-500 pts. wt. silkworm dropping.    USE - The fertilizer is useful for sugarcane (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves fermenting livestock manure, plant ash and silkworm dropping for 3-5 months, mixing fermented product with peanut, crushing obtained mixture to obtain powder having particle diameter of 200-300 mu m, mixing the powder with the potassium nitrate, borax, manganese sulfate and zinc sulfate, uniformly mixing and stirring mixture, granulating the mixture using granulator, and drying granules at 80-100 degrees C to obtain product.
NOVELTY - Fertilizer comprises 80-100 pts. mass urea, 20-30 pts. mass calcium superphosphate, 12-14 pts. mass calcium-magnesia phosphate fertilizer, 30-40 pts. mass paddy, 50-70 pts. mass seatangle, 30-40 pts. mass chicken manure, 60-80 pts. mass dairy manure, 30-50 pts. mass lees, 10-12 pts. mass fungus powder, 18-20 pts. mass bentonite, and 100-120 pts. mass water.    USE - As fertilizer for ryegrass (claimed).    ADVANTAGE - The fertilizer is prepared simply, and improves nitrogen content in the soil, and quality of the ryegrass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves mixing the above-mentioned raw materials, crushing the mixture, adding 100-120 pts. wt. water to the mixture, uniformly stirring the mixture, sealing and fermenting the stirred mixture for 4-6 days, and granulating the obtained fermented mixture using granulator.
NOVELTY - Production of ammonium dihydrogen phosphate eggplant fertilizer comprises mixing phosphoric acid and urea, heating, reacting under stirring condition, obtaining urea phosphate slurry, slowly adding ammonium hydroxide, regulating pH, fully stirring, obtaining material slurry containing nitrogen and phosphorus, adding material slurry into cooling crystallizer, cooling, filtering, separating ammonium dihydrogen phosphate, adding the filtrate with trace element and potassium element, obtaining mother liquid, drying, and controlling water content.    USE - Production of ammonium dihydrogen phosphate special eggplant fertilizer (claimed).    ADVANTAGE - The method provides high purity ammonium dihydrogen phosphate, has reduced cost, provides fertilizer which provides the maximum content of nutrients needed by eggplant, reduces waste of element, and avoids soil pollution caused by fertilizer residue.    DETAILED DESCRIPTION - Production of ammonium dihydrogen phosphate eggplant fertilizer comprises mixing phosphoric acid and urea at 1.8-2.2:1.4-1.6 mol ratio, where phosphoric acid concentration is 65-75%, heating at 8 degrees C/minute to 85-120 degrees C and reacting while stirring for 20 minutes to obtain urea phosphate slurry, slowly adding ammonium hydroxide, regulating pH at 3.4-3.7, fully stirring, obtaining material slurry containing nitrogen and phosphorus, adding material slurry into cooling crystallizer, cooling to 18-24 degrees C, filtering, separating ammonium dihydrogen phosphate, adding trace element and potassium element to the filtrate, obtaining mother liquid, drying in drying machine at controlled temperature of 33-36 degrees C for 25-30 minutes, and controlling water content of eggplant fertilizer at 3-5%.
NOVELTY - Spirodiclofen is synthesized by reacting 3-(2,4-dichlorophenyl)-2-oxo-1-oxa-spiro(4,5)-dec-3-ene-4-ol and spirodiclofen in presence of triethylamine catalyst in aprotic organic solvent, adjusting pH to 10-11 using alkaline solution, standing to form layers to obtain aqueous phase and organic phase, recycling water phase as alkaline solution, washing organic phase with water, drying over anhydrous sodium sulfate, distilling under atmospheric pressure to remove mixed solvent containing triethylamine and aprotic organic solvent, recycling mixed solvent, and recrystallizing solid product.    USE - Synthesis of spirodiclofen (claimed).    ADVANTAGE - Process recovers catalyst and organic solvent, and has reduced cost, reduced emission of highly concentrated salt water and wastewater, and increased yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of synthesis of spirodiclofen. (Drawing includes non-English language text).
NOVELTY - Method for fermenting sugar by acetone-butanol-ethanol (ABE) fermentation, involves performing enzymolysis of crop waste comprising sugar and sugar solution, collecting product, adding nutritional salt to the product, and performing fermentation.    USE - The method for fermenting sugar by ABE fermentation (claimed), and fibers and lignin.    ADVANTAGE - The method degrades sugar that is difficult to degrade, is environmentally-friendly and economically beneficial, and completely utilizes biomass.
NOVELTY - Extracting and separating sinomenine comprises taking caulis sinomenii raw powder as raw material, adding slaked lime, mixing, spraying water to wet, alkalizing, placing the raw material in an extraction tank, adding ethyl acetate as solvent, reflowing and extracting, filtering the extract liquid, placing in a concentrating tank for concentrating under vacuum condition, placing the concentrated liquid in the extracting tank, adding hydrochloric acid to adjust pH, removing out hydrochloric acid layer, using activated carbon to decolor, regulating pH, placing for overnight, and separating out.    USE - The method is useful for extracting and separating sinomenine (claimed).    ADVANTAGE - The method: is environmentally-friendly and industrialized (claimed); utilizes ethyl acetate as extraction solvent to replace traditional benzene extraction with large toxicity or chloroform extraction; and solves the problems of environmental pollution and health hazards to animals and humans by the existing technology.    DETAILED DESCRIPTION - Extracting and separating sinomenine comprises taking caulis sinomenii raw powder as raw material, adding slaked lime, which is 10 wt.% of the raw material, mixing uniformly, spraying water to wet, allowing to stand for many hours, alkalizing, placing the raw material in an extraction tank, adding specific amount of ethyl acetate as solvent, reflowing and extracting for 3 times, filtering the extract liquid through a suction filter, placing in a concentrating tank for concentrating under vacuum condition, placing the concentrated liquid in the extracting tank, adding hydrochloric acid to adjust pH to 4-5, removing out hydrochloric acid layer, using activated carbon to decolor, regulating pH to 2, placing for overnight, and separating out sinomenine hydrochloride.
NOVELTY - Utilization of combustion exhaust gas to promote aerobic fermentation reaction is carried out by using waste heat and exhaust gas generated from fuel combustion to heat a reactor for fermentation reaction of organic waste, in which part of chemical substances in organic waste is absorbed on the exhaust gas.    USE - Method for utilizing combustion exhaust gas to promote aerobic fermentation reaction (claimed).    ADVANTAGE - The method can save treatment system of exhaust gas and use of combustion device, thus reducing cost. It can increase aerobic fermentation efficiency of organic waste and shorten fermentation time, and is environment-friendly and energy-saving.
NOVELTY - Producing ethyl alcohol fuel using chaff, comprises (i) taking mildew-free chaff, cleaning, dissolving in water and heating for 40-60 minutes at 40-50 degrees C, (ii) adding calcium hydroxide powder and heating, (iii) adding 8-10 mu /g alpha -amylase and liquefying to obtain mash liquid, (iv) adding sodium carbonate powder, reacting, filtering and removing residue to obtain filtered liquid, (v) transferring filtered liquid into a fermentation jar, adding saccharifying enzyme and yeast, saccharifying, and anaerobic fermenting to obtain fermentation liquid of ethyl alcohol, and (vi) distilling.    USE - The method is useful for producing ethyl alcohol fuel using chaff (claimed).    ADVANTAGE - The method solves environmental pollution problem and waste of energy, is simple and economical, and has high product conversion rate.    DETAILED DESCRIPTION - Producing ethyl alcohol fuel using chaff, comprises (i) taking mildew-free chaff, cleaning, dissolving in water of solid-liquid ratio 1:10-1:15 and heating for 40-60 minutes at 40-50 degrees C, (ii) adding calcium hydroxide powder and heating to 60-80 degrees C for 4-5 days, where the mass ratio of chaff and calcium hydroxide is 100:1-50:1, (iii) adding 8-10 mu /g alpha -amylase and liquefying at 90 degrees C for 5-6 hours to obtain mash liquid, (iv) adding sodium carbonate powder according to 1.5-2 times of calcium hydroxide, reacting for 1-2 hours, filtering and removing residue to obtain filtered liquid, (v) transferring filtered liquid into a fermentation jar, adding 60-100 U/g saccharifying enzyme and 5-10% yeast, saccharifying at 30-35 degrees C, and anaerobic fermenting under sealed condition for 70-90 hours to obtain fermentation liquid of ethyl alcohol, and (vi) distilling.
NOVELTY - The device has separating tank (124) that is inclinedly set at pedestal (121) and is provided on conveying unit (123). The connection of separate motor (122) and stir stick (126) is made to drive stir stick to be rotated. The conveyer belt (127) is provided at isolation network (128) and is set with transmission wheel. The conveying electric machine is provided for driving transmission wheel using conveyer belt. The top portion of the tank is set with spore outlet (1251). The spore outlet is connected with the transmission wheel through top conveyer belt.    USE - Spore separating device for production of organic fertilizer.    ADVANTAGE - The separation of spore can be made easily. The spore separating device is simple in structure, convenient to use, high in productivity, low in cost, and high in production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the spore separating device.    Pedestal (121)    Separate motor (122)    Conveying unit (123)    Separating tank (124)    Stir stick (126)    Conveyer belt (127)    Isolation network (128)    Spore outlet (1251)
NOVELTY - Extraction of levodopa involves crushing velvet beans, placing in a high-pressure tank, adding pure water, pressurizing at 4 kgf/cm2 for 10-15 minutes, filtering, extracting, obtaining lower extraction phase and aqueous two-phase extraction phase containing 20-30 %mass polyethylene glycol, 1-5 %mass sodium hydroxide and remainder of water, desalinating, crystallizing, and drying. The weight average molecular weight of polyethylene glycol is 1000-8000.    USE - Extraction of levodopa (claimed).    ADVANTAGE - The levodopa is extracted with high extraction rate, by simple and economical process.
NOVELTY - Invention relates to method of obtaining low-pressure hydrogen for further combustion and obtaining water vapour by means of low-voltage electrolysis of alkaline electrolyte of solution of salts of hydrohalic acids and their mixtures by constant current, by means of aluminium electrodes, with further extraction of oxygen from formed aluminium complexes into separate accumulating tank, with support of electrolyte composition and temperature and pressure control in electrochemical cell.    USE - Chemistry.    ADVANTAGE - Application of claimed method makes it possible to reduce danger in carrying out the process due to binding of resulting from reaction oxygen into complexes and possibility of its further utilisation.3 dwg
NOVELTY - Supported catalyst comprises a carrier and a metallic active component supported on the carrier. The metallic active component comprises 0.5-20% zinc oxide and 10-50% zinc halide, and the content of the carrier is 40-88%.    USE - The catalyst is useful for converting halomethane into isobutylene (claimed).    ADVANTAGE - The catalyst: can convert halomethane into isobutylene with high selectivity, preferably preparing isobutylene by converting bromomethane with bromomethane conversion of not less than 90% and isobutylene selectivity of not less than 80%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparation of the supported catalyst, comprising introducing zinc oxide into a carrier, and carrying out halogenations; and    (2) preparing isobutylene from halomethane, comprising reducing load type catalyst by hydrogen, activating, such that the halogen content of the catalyst is reduced to 20-90% of the total halogen content of the catalyst precursor, contacting the catalyst with halomethane to prepare isobutylene.
NOVELTY - Preparation of cyclopropane ring-bearing compound (I) involves reacting alkyl group-containing compound (II) with nucleofuge-containing compound (III) in the presence of a metal catalyst complex chosen from catalyst for catalytic cyclopropanation reaction and catalyst for Heck coupling reaction.    USE - Preparation of cyclopropane ring-bearing compound used as intermediate for synthesizing pharmaceutical, agrochemical, flavor, and fragrances.    ADVANTAGE - The method enables preparation of cyclopropane ring-bearing compound with high yield and reduced generation of zinc-containing waste, by economical process.    DETAILED DESCRIPTION - Preparation of cyclopropane ring-bearing compound of formula (I) involves reacting alkyl group-containing compound of formula: R1-HC=CH-R2 (II) with nucleofuge-containing compound of formula: X-CH2-Y' (III) in the presence of a metal catalyst complex chosen from catalyst for catalytic cyclopropanation reaction and catalyst for Heck coupling reaction.    R1,R2=optionally substituted 1-10C alkyl;    R1+R2=monocyclic or bicyclic ring system containing heteroatom;    X=nucleofuge chosen from halide or pseudohalide;and    Y'=electrofuge chosen from borane or borate.
NOVELTY - Manufacture of lacosamide compound (I) involves reacting (2R)-2-(acetylamino)-3-hydroxypropanoic acid (II) with a methylating agent in presence of an inorganic lithium compound and producing a (2R)-2-(acetylamino)-3-methoxypropanoic acid compound (III).    USE - Manufacture of lacosamide compound used as analgesic and anticonvulsant.    ADVANTAGE - The method enables manufacture of lacosamide compound with high chiral purity and productivity, by simple and environmentally-friendly process, without using catalyst such as organic solvent.    DETAILED DESCRIPTION - Manufacture of lacosamide compound of formula (I) involves reacting (2R)-2-(acetylamino)-3-hydroxypropanoic acid of formula (II) with a methylating agent in presence of an inorganic lithium compound and producing a (2R)-2-(acetylamino)-3-methoxypropanoic acid compound of formula (III).    Bn=benzyl.
NOVELTY - Method of production of plant growth stimulant is carried out by hydrolysis of cattle manure under aerobic and anaerobic conditions, using the seed material at different stages of the technological process of specially selected associations of lactobacilli and indigenous methanogenic microorganisms. All stages of the technological process are carried out continuously using a detachable-filling technology of the process that provides complete replacement of raw material in the bioreactor for 7-10 days.    USE - Agriculture.    ADVANTAGE - Obtaining liquid organic fertilisers, disinfected from pathogenic microflora, free from weed seeds and with low odour threshold, complete preservation of nutrients which are in the initial manure drain by storing all nitrogen in ammonium or organic forms, phosphorus is mainly in the form of phosphatites and nucleoproteins, and potassium is in the form of soluble salts, which provides their better accessibility by plants.3 cl, 2 tbl
NOVELTY - The method involves positioning gas diffusion layers (12b,13b) to each of electrode catalyst layers (12a,13a). A solid polymer electrolyte membrane (11) is supplied on any one electrode catalyst layer of an anode (12) and a cathode (13) by a supply unit. The solid polymer electrolyte membrane is positioned along the unevenness of surface of electrode catalyst layer, by pressurizing by a pressurizing unit and performing cladding.    USE - Manufacturing method of fuel cell membrane electrode composite-portion.    ADVANTAGE - The wrinkles of membrane is avoided, and thus the membrane electrode assembly (MEA) is formed cheaply at high-speed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the polymer electrolyte fuel cell stack provided with the membrane electrode assembly.    Solid polymer electrolyte membrane (11)    Anode (12)    Electrode catalyst layers (12a,13a)    Gas diffusion layer (12b,13b)    Cathode (13)    Membrane electrode assembly (20)
NOVELTY - The device has a boost converter connected to a fuel cell and controlling load voltage at a normal operation mode. A digital signal processing unit is connected between a load and the fuel cell. The digital signal processing unit detects output response of the fuel cell. A supplementary energy storage device discharges electricity from the fuel cell. The digital signal processing unit handles sudden change or instantaneously overload of the load. A bidirectional converter extracts impedance parameter and estimates lifetime of the fuel cell according to the impedance parameter.    USE - Power conversion device for a fuel cell.    ADVANTAGE - The device implements load leveling function for easily diagnosing lifetime of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a power conversion device of a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a power conversion device.'(Drawing includes non-English language text)'
NOVELTY - The device has a waste pre-processing system (13) that comprises a domestic garbage bin (2), a stirring system (12), an organic garbage hydrolysis pool (4) and an inorganic garbage storage pool (6). The inorganic garbage storage pool is set on one side of organic garbage hydrolysis pool. The organic garbage hydrolysis pool is connected with sewage anaerobic fermentation pool (15) whose top portion is provided with an air outlet (16). The sewage anaerobic fermentation pool is connected with the secondary level sewage treatment pool (21) through sewage flow or overflow pipeline (18).    USE - Scattered type rural household waste resource recycling device.    ADVANTAGE - The recycling operation is performed simply and conveniently. The operation cost is reduced. The solid waste reduction rate is more than 40%. The domestic garbage collection and conveying cost is greatly reduced. The maintenance cost is reduced.    DETAILED DESCRIPTION - A stirring system is arranged on domestic garbage bin or organic garbage hydrolysis pool. The stirring system is provided with a domestic sewage water inlet (9). An INDEPENDENT CLAIM is included for scattered type rural household waste resource recycling method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the scattered type rural household waste resource recycling device.    Domestic garbage bin (2)    Organic garbage hydrolysis pool (4)    Inorganic garbage storage pool (6)    Domestic sewage water inlet (9)    Stirring system (12)    Waste pre-processing system (13)    Sewage anaerobic fermentation pool (15)    Air outlet (16)    Overflow pipeline (18)    Secondary level sewage treatment pool (21)
NOVELTY - Preparation of polyvinyl chloride copolymer resin involves adding deionized water and initiator to reactor, purging nitrogen, adding polyvinylidene chloride, co-monomer and crosslinking agent, stirring, heating at 50-80 degrees C for 12 hours, drying, crushing resultant product, adding foaming agent, stirring, heating and cooling.    USE - Preparation of polyvinyl chloride copolymer resin (claimed).    ADVANTAGE - The method enables simple preparation of polyvinyl chloride copolymer resin having excellent barrier property, flame retardance and mechanical strength, with high yield.
NOVELTY - A fiber-based three-dimensional porous material comprises biomass fiber crosslinked to support three-dimensional network structure.    USE - Fiber-based three-dimensional porous material is used in biomedical application and aerospace application.    ADVANTAGE - The fiber-based three-dimensional porous material is manufactured by simple, environmentally-friendly and economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fiber-based three-dimensional porous material, which involves using crosslinking agent.
NOVELTY - A Chinese rose fertilizer comprises 10-14 pts. wt. soybean meal, 11-15 pts. wt. colza cake, 8-10 pts. wt. sesame cake powder, 10-14 pts. wt. peanut cake powder, 4-6 pts. wt. medical stone, 8-12 pts. wt. dry chicken manure, 8-10 pts. wt. dry cow manure, 8-9 pts. wt. dry goose manure, 10-13 pts. wt. pulverized coal ash, 6-10 pts. wt. phosphate, 1-1.5 pts. wt. saw dust, 0.3-0.5 pt. wt. paclobutrazol and 0.2-0.5 pt. wt. insecticide.    USE - Chinese rose fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Chinese rose fertilizer comprising taking raw materials, stirring, crushing, fermenting for 60 hours, adding 20 wt.% human excrement, turning, fermenting for 60 hours at 70 degrees C, adding 20 wt.% human excrement, turning 5 times, molding, and pressing.
NOVELTY - An organic garbage deodorant comprises 10-20 pts. wt. Bacillus subtilis, 10-25 pts. wt. Bacillus licheniformis, 10-25 pts. wt. yeast, 5-15 pts. wt. nitrobacteria, 8-20 pts. wt. Lactobacillus, 10-20 pts. wt. sulfur bacterium, 15-30 pts. wt. Streptomyces and 10-25 pts. wt. Trichoderma viride.    USE - Organic garbage deodorant for reducing composite bacteria.    ADVANTAGE - The organic garbage deodorant has high efficiency, wide adaptability and reduced cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic garbage deodorant, which involves inoculating the Bacillus subtilis, Bacillus licheniformis, yeast, nitrobacteria, Lactobacillus, sulfur bacterium, Streptomyces and Trichoderma viride strain into the activated culture medium to obtain seed liquid, followed by drying the liquid to obtain powder as finished product.
NOVELTY - A straw is reused by: cutting straw, and soaking into boiling water with acetic acid; washing with water, drying, adding dilute sulfuric acid, injecting into Soxhlet extractor, continuously reflux extracting, and filtering to obtain filtrate; adding calcium hydroxide, stirring, precipitating, filtering, and concentrating to obtain lignocellulose solution; adding cellulase, stirring, and saccharifying to obtain sugar liquid; and soaking filtrate into ammonia water, clean water washing, pulverizing into powder, adding dried corn, and mixing uniformly to obtain poultry feed.    USE - Method for reusing straw (claimed).    ADVANTAGE - The method is energy-saving and environment-friendly. The feed is easy to digest.    DETAILED DESCRIPTION - A straw is reused by:    (A) cutting straw into length of 3-5 cm, and soaking into boiling water with acetic acid at 100 degrees C for 15 minutes;    (B) 3-5 times washing with water, drying for 2-3 hours, adding 1 mol dilute sulfuric acid, injecting into Soxhlet extractor, continuously reflux extracting at 80-120 degrees C for 3-10 hours, and filtering to obtain filtrate;    (C) adding calcium hydroxide, stirring at 100 degrees C, precipitating, filtering, and concentrating to obtain lignocellulose solution;    (D) adding cellulase, stirring at 35-45 degrees C, and saccharifying to obtain sugar liquid;    (E) soaking filtrate into ammonia water for 30 minutes, 3-5 times clean water washing, pulverizing into powder, adding dried corn, and mixing uniformly to obtain poultry feed; and    (F) filtering lignocellulose solution, cleaning with water, dehydration drying, and gauze packing.
NOVELTY - An Eucommia ulmoides powder-containing organic compound fertilizer contains wheat straw, chicken essence, sheep essence, Physalis, Evodia rutaecarpa fruit extract, Pseudolarix, berberine, Forsythia, Astragalus complanatus, Murraya paniculata, Inula cuspidata, Eucommia ulmoides leaf powder, Carpesium abrotanoides, Lobelia, Angelica, radix polygonati officinalis, silver lace vine, and Rhizome kaempferiae.    USE - Eucommia ulmoides powder-containing organic compound fertilizer (claimed).    ADVANTAGE - The Eucommia ulmoides powder-containing organic compound fertilizer has pests-repelling effect, bacterial growth-inhibition effect and does not contains Chinese alkaline substances and other active substances which damages cell membranes.    DETAILED DESCRIPTION - An Eucommia ulmoides powder-containing organic compound fertilizer comprises 200-250 pts. wt. wheat straw, 150-200 pts. wt. chicken essence, 150-200 pts. wt. sheep essence, 1-2 pts. wt. Physalis, 1-2 pts. wt. Evodia rutaecarpa fruit extract, 2-3 pts. wt. Pseudolarix, 1-2 pts. wt. berberine, 1-2 pts. wt. Forsythia, 2-3 pts. wt. Astragalus complanatus, 1-2 pts. wt. Murraya paniculata, 2-3 pts. wt. Inula cuspidata, 3-6 pts. wt. Eucommia ulmoides leaf powder, 1-2 pts. wt. Carpesium abrotanoides, 2-3 pts. wt. Lobelia, 2-3 pts. wt. Angelica, 2-3 pts. wt. radix polygonati officinalis, 1-2 pts. wt. silver lace vine, 2-4 pts. wt. Rhizome kaempferiae, 1-2 pts. wt. Kaempferol, 1-2 pts. wt. pomegranate rind, 60-80 pts. wt. monoammonium phosphate, 40-50 pts. wt. polyaspartic acid, 40-60 pts. wt. potassium chloride and 50-60 pts. wt. magnesium sulfate. An INDEPENDENT CLAIM is included for preparation of Eucommia ulmoides powder-containing organic compound fertilizer.
NOVELTY - Preparation of antioxidant extract comprises extracting using water as extracting solvent at normal temperature, removing contaminating proteins by thermal denaturation to improve the purity of superoxide dismutase, embedding pawpaw extract liquid with cyclic refined paste, freezing and drying to obtain dry extract powder.    USE - Method for preparing antioxidant extract (claimed).    ADVANTAGE - The method has low cost, and is environment-friendly.
NOVELTY - Preparation of hot pepper total saponin comprises taking hot pepper stem and leaf as raw material, drying, crushing into coarse powder, placing coarse powder into container, adding 30-80% aqueous alcohol solution at a solid-liquid ratio of 1:10-1:30, ultrasonically extracting at 25-70 degrees C, 40 Hz, and 400 W for 10-50 minutes, filtering, repeating for 1-3 times, filtering, combining hot pepper total saponin extracting liquids, vacuum concentrating to recover alcohol, and drying.    USE - Method for preparing hot pepper total saponin (claimed).    ADVANTAGE - The method is simple and suitable for industrial production, and has short time period, high efficiency, low cost, low energy consumption, and no pollution.
NOVELTY - The device has a waste gas treatment box body formed with a waste pneuma outlet. An inner part of a slide rail is connected with the waste gas treatment box body. The slide rail is arranged with a mold. The slide rail is equipped with an electrode that is connected with an outlet end of the mold. An end of the mold is arranged with a pushing lifting platform that is connected with a hydraulic pressure oil jar. A lower moving platform is connected with a bearing surface that is mounted with a pushing device and the slide rail.    USE - Low temperature plasma waste gas processing device.    ADVANTAGE - The device is simple in structure, and reduces labor intensity and platform work area and increases working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a low temperature plasma waste gas processing device.
NOVELTY - A cobalt-based catalyst is porous transition metal composite oxide catalyst comprising mesoporous material assembled from nanocrystals and catalyst component chosen from ferrite, cobalt oxide, nickel oxide and/or manganese oxide. The catalyst has specific surface area of 23.38-172.28 m2/g and grain size of 4.5-15.5 nm.    USE - Cobalt-based catalyst used in preparation of methane and carbon monoxide catalyst material (claimed).    ADVANTAGE - The cobalt-based catalyst has large specific surface area, size, composition, texture and controllable parameters, and is manufactured economically by a simple and easy process. The catalyst effectively reduces methane ignition temperature, improves methane combustion rate and provides excellent low-temperature catalytic material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the cobalt-based catalyst.
NOVELTY - Invention relates to ecology. For disposal of metallurgical wastes including heavy metals, slime is carried and sorted out with separation of uncomposted fractions and biochemical enrichment of residual fraction to get biomineral fertiliser. Slime solid fractions are minced by dispersion in fluid to get the pulp to be subjected to ultrasound processing for at least 3 hours at 20-30 degrees C and, additionally, biochemically processed organic mass is added thereto. For compost fermentation, air heated to 35 degrees C to 45 degrees C is fed. Formed sediment with radio nuclides and heavy metals are separated, dewatered and directed for further processing or burial.    USE - Process engineering.    ADVANTAGE - Simplified process.2 cl, 9 tbl, 6 ex
NOVELTY - The method involves measuring (S11) electric current flowing between a cathode plate and an anode plate. The discharging water flow volume of hydrogenous water produced in a cathode chamber is measured (S12). The dissolved hydrogen concentration in the hydrogenous water produced in the cathode chamber is computed (S13) according to the electric current and discharging water flow volume based on the data showing correlation between the measured electric current and the discharging water flow volume.    USE - Method for measuring dissolved hydrogen concentration in the electrolytic hydrogen water.    ADVANTAGE - The discharging water flow volume of hydrogenous water produced in a cathode chamber is measured which ensures that the dissolved hydrogen concentration in the electrolytic hydrogen water is measured in a convieninet manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolyzed water generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a method for measuring dissolved hydrogen concentration in the electrolytic hydrogen water. (Drawing includes non-English language text).    Applying voltage between a cathode plate and an anode plate (S10)    Measuring electric current flowing between a cathode plate and an anode plate (S11)    Measuring discharging water flow volume of hydrogenous water produced in a cathode chamber (S12)    Computing dissolved hydrogen concentration in the hydrogenous water produced in the cathode chamber (S13)
NOVELTY - A multifunctional detecting box, the box body (1) box wall is set with outside screw thread, through a transverse through hole and a chip through hole, the transverse through tube (2) is provided with a inlet and a groove, the transverse through tube (2) one end is mounted in a box body (1), a transverse through tube (2) of the box body (1) is a transverse through a upper box wall through hole in the vertical through tube (3) one end of a transverse through tube (2) on inlet of the cover body (4) is provided with inner screw thread, a cover body (4) is inner screw thread and the box body (1) is a outside screw thread, one end straight through pipe (5) is mounted in a cover body (4), and the vertical through tube (3) in the inner straight pipe (5) of another end of the transverse inlet through a 2, this utility new type has advantages is: at the same time more rapid pathogen, structure is simple, operation is convenient, also continuous use, energy-saving and environment-friendly.
NOVELTY - The utility model claims a biogas digester for making biogas slurry and biogas residue reflow using air pressure, comprising a body, an anchoring groove, a drain pipe, a biogas backflow pipe, a pneuma pipe, discharging pipe and slag reflux pipe; on the pneuma conveying pipe provided with a gas multi-branch pipe A and supporting pipe B, a gas discharging pipe A a connection to a body, another end connected to discharging liquid sand well, the biogas slurry refluxing tube one end connected to a body, another end connected to biogas slurry reflowing sand well, reflux tube and input branch tube A connected pneuma, between liquid return pipe and liquid discharging pipe set with biogas distribution pipe, said discharging pipe one end connecting to a body, and another end connected to the slag sand well, the biogas backflow pipe one end connecting to a body, another end connect to return sand well biogas residue, biogas backflow tube and input branch tube B connected pneuma, between residue return pipe and discharging pipe set with biogas distribution pipe, the marsh gas pool by reflux of biogas slurry and biogas residue, which is good for uniformity of fermentation material to prevent the upper shell structure.
NOVELTY - This utility new type claims a uniform a marsh gas collection system, a gas collecting pipe, a pneuma drainage sand well, aspirated and pressurizing air storage device, a gas collecting tube mounting arrangement in marsh gas pool surface periphery, a collecting pneuma drainage sand well equipped with a biogas pool; the pressurizing air storage device b. marsh gas pool outside; the gas collecting tube across set pneuma drainage sand well. b pressurizing air storage device; the aspirated mounting a gas collecting tube a. The uniform collection marsh gas system using PVC pipe annular mounting arrangement, simple structure, corrosion resistance, surface drill pipe size same hole, which ensures the whole marsh gas a uniform air flow entering into collecting pipe, collection efficiency is high.
NOVELTY - This new utility model claims of one of water slag completely separated marsh gas pool, comprising pool body, HDPE anti-seepage film top, air set air pipe, a water inlet pipe, a drain pipe and discharging, the pool body periphery is provided with periphery with anchor; the HDPE anti-seepage film top mounted on pool body upper part, the HDPE anti-infiltration membrane fixed in top anchoring groove; the marsh gas collected air tube is connected with air inlet at upper part of pool body; one end water inlet pipe is connected at the middle part of pool body; one end arrange water pipe and the middle part is connected with the pool body, the drain pipe and the water inlet pipe and the other relative side, the discharging pipe one end is connected with pool body bottom, the other end is connected with slag sand well arrange, and arrange slag sand by using biogas residue discharging well. The water slag completely separated biogas pool structure is simple, can effective separate the water slag in the marsh gas pool, marsh gas pool using further large play to the efficiency and greatly increase utilization rate of the marsh gas pool.
NOVELTY - Recovery of methane gas involves applying a mixed gas comprising natural gas hydrate, carbon dioxide and nitrogen, and additive gas, and recovering methane gas using mixed gas. The addition of gas phase equilibrium curve of nitrogen-carbon dioxide is more than the phase-equilibrium curve of mixed gas which is provided in the right area.    USE - Recovery of methane gas from natural gas hydrate (claimed).
NOVELTY - A cyclooctyloxy acetamide compound is new.    USE - A cyclooctyloxy acetamide compound used as chemical linkage reagents for measuring interactions between affinity molecule and its targeting biomolecules.    ADVANTAGE - Preparation process is environment-friendly and easy to operate and has high yields.    DETAILED DESCRIPTION - A cyclooctyloxy acetamide compound of formula (I) is new.    X,Y'=O, CH2, NH, or NCH3;    P'=CH2 or O; and    s,t=0-5.    INDEPENDENT CLAIMS are included for:    (1) compound of formula (III);    (2) compound of formula (IV);    (3) compound of formula (V);    (4) composition containing compounds of formulae (I) or (III);    (5) kit comprising compounds of formulae (I)-(V) and (3);    (6) kit comprising the composition;    (7) preparation of cyclooctyloxy acetamide compound of formula (I);    (8) preparation of compound of formula N3-(CH2CH2-O)12-CH2CH2-S(=O)2-CH=CH2 (6a) which involves mixing hexaethylene glycol and compound of formula N3-(CH2CH2-O)6-Ts (4) in the presence of 1st base to form compound of formula (5) N3-(CH2CH2-O)12-H and mixing divinyl sulfone, compound (5), and a 2nd base;    (9) preparation of compound of formula N3-(CH2CH2-O)36-CH2CH2-S(=O)2-CH=CH2 (6b) which involves mixing compound N3-(CH2CH2-O)36-H, divinyl sulfone, and tert.-butoxide;    (10) method of attaching affinity molecule to molecule linker which involves contacting nucleophilic moiety of affinity molecule to molecular linker in aqueous medium;    (11) preparation of immobilized affinity molecules attached to functionalized atomic force microscope (AFM) tip which involves mixing AFM tip with compound of formula (I); and    (12) functionalization of AFM which involves reacting silatrane moiety of compound (I) with silanol on surface of AFM tip.    A=CH2 or O; and    u=1-36.
NOVELTY - A fuberidazole is prepared by mixing rice and wheat with organic solvent, dehydrating, adding carrier solvent, heating by evaporation or distillation, grinding, and packaging.    USE - Method for preparing fuberidazole (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - This utility new type relates to medical appliance technology field, specifically relates to a microelectronics a medical magnetic treating instrument. This utility new type through a traditional Chinese medicine in a traditional Chinese medicine bag set in electromagnetic field, and using the human body self-weak electric, a electromagnetic field for traditional Chinese medicine in a traditional Chinese medicine is a medicine bag by heating after a accelerate volatile traditional Chinese medicine, traditional Chinese medicine molecule is affected by a magnetic force line for leading-in human body, part medicine for spreading a peripheral space b, form for treating the human body health and environment protection.
NOVELTY - A Bacillus sp. strain SCH-1 capable of producing chitinase in saline medium, is new.    USE - The Bacillus sp. strain SCH-1 is useful for producing chitinase, and in composition for degrading food waste (all claimed).
NOVELTY - Paenibacillus lautus sp. nov. SCH-2 (KCTC 33051) strain, is new.    USE - The strain is useful in composition for decomposing food waste (claimed).    ADVANTAGE - The strain exhibits enzymatic activity in the culture medium containing salt, and has chitinase production capacity (claimed) and excellent chitin decomposition capability; and shorts the fermentation period of fermented food.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (I) chitinase produced by SCH-2 strain; and #composition comprising SCH-2 strain or its cultures product.
NOVELTY - The electrode comprises a separation film and a nano pattern that is formed on the separation film through a nano imprint lithography process, where an air cathode is also provided.    USE - Electrode for microbial fuel cell (claimed) for producing current.    ADVANTAGE - The electrode comprises a separation film and a nano pattern that is formed on the separation film through a nano imprint lithography process, and thus efficiently produces current.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing separation film of an electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of difference of the maximum electrode efficiency of the membrane electrode assembly.
NOVELTY - The apparatus has a storage tank (10) that is accommodated inside the vessel and is generated with volatile organic compound (VOC) inside. A reforming reactor (20) reacts and reforms volatile organic compound (VOC) with the steam for producing methane. The storage tank is provided for storing oil or the liquefied gas. The reforming reactor is provided with supply unit for supplying generated hydrocarbon to the storage tank during cooling process of methane.    USE - Apparatus for decreasing volatile organic compound (VOC) using steam modification, mounted in vessel.    ADVANTAGE - The VOC generated in the storage tank of the vessel using the steam modification can be reduced. The VOC using steam modification can be used as fuel including the engine of the vessel or the generator, so that the methane can be efficiently generated in the reduction process.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the apparatus for decreasing VOC. (Drawing includes non-English language text)    Liquefied material (5)    Storage tank (10)    Reforming reactor (20)    Combustor (30)    Steam feeder (40)
NOVELTY - Culturing microorganisms for producing ethene.    USE - The method is useful for culturing microorganisms for producing ethane (claimed).    ADVANTAGE - The method: utilizes renewable raw materials; and produces 3 times more yields of ethylene and propylene.
NOVELTY - Preparation of soluble citrate salt comprises taking citric acid, adding metal organic salt or inorganic salt, mixing and reacting.    USE - Method for preparing soluble citrate salt, particularly potassium citrate, magnesium citrate, ferric citrate, strontium citrate, lanthanum citrate, ammonium ferric citrate and zinc citrate (claimed).    ADVANTAGE - The citrate salt has purity of greater than or equal to 98% and solubility in purified water of greater than or equal to 3 g/100 mL at 25 degrees C. The method is simple and environment-friendly, and has low energy consumption, short production cycle and low production cost.
NOVELTY - Preparation of high purity fudosteine includes dissolving 1,3-propanediol and hydrobromide in hydrocarbon solvent, refluxing in the presence of bromine salt catalyst, monitoring gas phase reaction, separating upper end layer of reaction solvent, adjusting pH with alkali liquid, and distilling; and homogeneously reacting with cysteine hydrochloride and sodium hydroxide, monitoring liquid phase reaction, adjusting pH with acid, concentrating solvent under reduced pressure, desalinating with aqueous ethanol solution, washing with water, and crystallizing with ethanol.    USE - Method for preparation of high purity fudosteine (claimed).    ADVANTAGE - The method is suitable for industrial production, utilizes inexpensive and easy to obtain raw materials, and it has high selectivity, low pollution and cost, and stable quality.    DETAILED DESCRIPTION - Preparation of high purity fudosteine comprises dissolving 1,3-propanediol and hydrobromide in hydrocarbon solvent, refluxing in the presence of bromine salt catalyst, monitoring gas phase reaction, separating upper end layer of reaction solvent, adjusting pH with alkali liquid, and distilling under reduced pressure to obtain high-purity 3-bromopropanol; and homogeneously reacting with cysteine hydrochloride and sodium hydroxide, monitoring liquid phase reaction, adjusting pH with acid, concentrating solvent under reduced pressure, desalinating with aqueous ethanol solution to obtain crude fudosteine, dissolving in water, and crystallizing with ethanol.
NOVELTY - Production of levosimendan (I) comprises taking 6-(4-aminophenyl)-5-methyl-4,5-dihydro-3(2H)-pyridazinone (II) as starting material, carrying out chiral separation with L-tartrate and sodium nitrite, and reacting with dilute nitric acid and malononitrile.    USE - Method for producing levosimendan (claimed).    ADVANTAGE - The method produces product with high yield and optical purity and has low cost and good environmental protection.    DETAILED DESCRIPTION - Production of levosimendan (I) comprises taking 6-(4-aminophenyl)-5-methyl-4,5-dihydro-3(2H)-pyridazinone (II) as starting material, carrying out chiral separation with L-tartrate and sodium nitrite, and reacting with dilute nitric acid and malononitrile.
NOVELTY - Preparation of imatinib mesylate comprises uniformly mixing imatinib base and organic solvent to obtain suspension-I; mixing aqueous solution of ammonia methanesulfonate and suspension-I, heating to 60-70 degrees C to carry out reaction, cooling, crystallizing, and filtering. The amount of organic solvent is 4-6 mL/g imatinib base. The amount of water in aqueous solution of ammonia methyl sulfonate is 1-2 mL/g imatinib.    USE - Method for preparing imatinib mesylate (claimed).    ADVANTAGE - The method is simple and environmental-friendly, has mild reaction condition, low requirements for equipment and low cost, and does not use methanesulfonic acid strong acid as raw material.
NOVELTY - Producing organic fertilizer microbial agent, comprises carrying out rapid fermentation of edible bacterial residue comprising high efficiency cellulose decomposing bacteria, high temperature actinomycetes, yeast and Lactobacillus, indigenous bacteria, Bacillus stearothermophilus strain having a preservation number of CGMCC NO: 1.1865.    USE - The method is useful for producing organic fertilizer microbial agent (claimed).    ADVANTAGE - The method shortens the composting time by 3-5 days, and produced product which meets the organic fertilizer standard (NY525-2012).
NOVELTY - Optimizing immobilization of calcified sodium alginate immobilized enzyme comprises supercritical carbon dioxide processing gel granule of calcium sodium alginate immobilized enzyme.    USE - The method is useful for optimizing immobilization of calcified sodium alginate immobilized enzyme (claimed).    ADVANTAGE - The method saves enzyme cost, does not use harmful substances, ensures easy operation, saves resources, and is environmentally friendly.
NOVELTY - This utility model claims a solar methane tank, comprising a feeding port, a feeding pipe, a fermentation, discharging hydraulic activity cover, seal cover, ring heating coil, insulation layer, solar energy pipe, solar energy heat collecting system, a heating plate pipe ring b. mounting a bottom part, ring heating tube lower plate has insulating layer, ring heating disk pipe through two pieces of solar energy pipe and solar energy heat-collecting system. The solar methane tank uses solar energy hot water supplied to a marsh gas pool technology modify technology is combined, by solar energy hot water circulation technology increase marsh gas pool gas yield in winter, marsh gas pool year reduce fluctuation range of air quantity, so as to increase the economic benefit.
NOVELTY - A dry anaerobic fermentation device using recovered biogas slurry spray straw relates to a dry anaerobic fermentation device, specifically relates to a dry anaerobic fermentation device using recovered biogas slurry spray straw. This utility model is that in present straw Anaerobic fermentation process of straw pre-processing stage and a stage must be separated from carrying out the process complicate, wasting time and in Anaerobic heat preservation character exist oxygen, incomplete fermentation, physics and high energy consumption problem. This utility model the biogas slurry feed pipe of another a livestock and poultry excrement and biogas liquid storage tank connected, reflux pump mounted in the feeding pipe a biogas, biogas slurry supplementing pipe plugging device in a livestock and poultry excrement biogas upper end of liquid storage tank, livestock and poultry excrement biogas liquid storage tank through lower end of biogas liquid discharge pipe and cabin body connected, marsh gas output pipe plugging is installed at upper end of chamber body in the air pipe from one side of plugging cabin is a cabin body. This utility model is used for agriculture marsh gas preparation.
NOVELTY - Composter (10), adapted to stand upright, includes a side wall that defines a compost-forming space, where the side wall (12) includes at least one region having an outer panel (16) and an inner panel (18) having a gap in between for air flow from outside the composter and through the gap into the compost forming space, an aerator for aerating the composting material and at least one divider (30) for partitioning the compost-forming space into at least two vertically spaced regions to control moisture and/or heat distribution between the spaced regions.    USE - The composter is useful for producing compost from household and other types of waste material (claimed).    ADVANTAGE - The composter enhances the formation of compost by aeration and is biodegradable and recyclable, thus minimizing the maintenance cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a kit for a composter comprises at least one blank which is foldable to form the outer panel of the side wall, and the inner panel of the side wall, where the inner panel has many openings in it; and    (2) an assembly of composters, where the side wall of the composter further includes at least one opening that is aligned with similar opening of a side wall of an adjacent composter to form passage for decomposers to travel between the composters.    DESCRIPTION OF DRAWING(S) - The figure illustrates an isometric view of the composter.    Composter (10)    Side wall (12)    Outer panel (16)    Inner panel (18)    Divider (30)
NOVELTY - The biodigester has a biogas tank (3c) arranged in a lower edge (5) of a roof cover that is fixed in an upper part of structural walls and a foundation (1) for receiving biomass. Wetting nozzles (7a) are located in a load biomass area with variable height by depending on height of a biomass load area. An intermediate area (1b) is located in the biomass load area. A pulp channel (2) is separated by a perforated partition (4) that is fixed in a bottom part of a biomass tank and forms a perforated pipe that is freely fixed suspended in a biomass layer.    USE - Biodigester for installing covers in a biogas fermentation chamber (claimed) for use in agriculture applications on individual farms.    ADVANTAGE - The biodigester allows proliferation of bacterial flora dissolved in organic compounds in an easy manner. The biodigester protects gas against destruction problems and controls humidity in interior of sleeve in an easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biodigester.    Foundation (1)    Intermediate area (1b)    Pulp channel (2)    Biogas tank (3c)    Perforated partition (4)    Lower edge (5)    Wetting nozzles (7a)
NOVELTY - The apparatus has an extermination tank (S) in which the food waste is stored. Multiple disks (130) are formed at the fixed interval in a rotary shaft (120) rotated with a drive motor. The fermentation gas is produced by mixing the food waste and the organic material is generated in the extermination tank so as to transfer from the top unit of multiple wings (140). A deodorization device transfers the food waste pushed by the extermination tank to the next stage through the sector-shaped space formed in inner wall portion of the extermination tank.    USE - Apparatus for treating food waste.    ADVANTAGE - The food waste is ejected in the state of the odorous gas by a deodorization device. The smooth transfer of the food waste is possible. The structure of apparatus is simple since the extermination tank formed in the inner structure of a housing. The configuration portions remove the generated odorous gas from the food waste after performing dehumidifying to the ozone oxidization, photooxidation and plasma method. Thus the deodorization efficiency of the odorous gas is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the apparatus for treating food waste. (Drawing includes non-English language text)    Housing (110)    Rotary shaft (120)    Disks (130)    Wings (140)    Extermination tank (S)
NOVELTY - The method involves carrying out disintegration successively in two steps with respect to the residues. The temperature of residual materials is increased with respect to the first portion of the residue, and mechanical disintegration in set temperature is carried out with respect to the second portion of the residue. The mechanical treatment step takes place in an ultrasonic system or a ball mill. The heating and mechanical disintegration processes are carried out simultaneously in a piece of equipment.    USE - Method for disintegration of organic residues such as sludge from biological wastewater or slurry of alcoholic fermentation.    ADVANTAGE - The hygiene effect is improved, while improving the efficiency by obtaining more amount of biogas and correspondingly less amount of mud. The thermal pretreatment stage is retrofitted with the disintegration installation in a simple manner.
NOVELTY - An assembly for generating eco-conscious products from waste using an anaerobic digester for anaerobically processing waste matter to produce anaerobic products selected from: biogas, liquid digestate, solid digestate, and mixtures, where one or more eco-assemblies receive the anaerobic products to generate at least one eco-conscious product, the eco-assemblies include one or more of an eco-matrix molder, an algae cultivator, a fast-pyrolysis chamber, a soil enhancer, a RDF pelletizer, and a hydroponic apparatus. Abstract based on disclosure.    USE - The assembly is useful for generating eco-conscious products from waste.    ADVANTAGE - The assembly can be efficiently used in generating eco-conscious products from waste, e.g. biogas, liquid digestate, solid digestate, and mixtures.    DETAILED DESCRIPTION - An assembly for generating eco-conscious products from waste using an anaerobic digester for anaerobically processing waste matter to produce anaerobic products selected from: biogas, liquid digestate, solid digestate, and mixtures, where one or more eco-assemblies receive the anaerobic products to generate at least one eco-conscious product, the eco-assemblies include one or more of an eco-matrix molder, an algae cultivator, a fast-pyrolysis chamber, a soil enhancer, a RDF pelletizer, and a hydroponic apparatus. Generating eco-conscious products from waste involves anaerobically processing waste matter to produce one or more of the anaerobic products, which are conveyed to one or more eco-assemblies to generate at least one eco-conscious product. Abstract based on disclosure.
NOVELTY - Preparing a herbicidally active carboxylic acid salt, comprises: (a) combining a carboxylic acid and an organic solvent having high boiling point and immiscible with water to obtain a solution or suspension; (b) treating the solution or suspension obtained in step (a) with a base to form a carboxylic acid salt; (c) removing the solvent from the mixture obtained in step (b) to obtain a cake of carboxylic acid salt; and (d) drying the obtained cake.    USE - The process is useful for preparing herbicidally active carboxylic acid salt, which is dicamba-sodium (claimed).    ADVANTAGE - The process utilizes low heating and drying conditions, and hence it is industrially scalable, economical, environmentally friendly and energy efficient, and provides the herbicidally active carboxylic acid salt in pure solid and free flowing form and that exhibits good solubility in water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the herbicidally active carboxylic acid salt prepared by the process.
NOVELTY - Dairy manure organic fertilizer comprises fresh cow dung, humic acid, bentonite, dry powder of turtle shell, rhizoma imperatae, cockscomb, wood shaving, lotus leaf, suberect spatholobus stem, pepper, seed of cowherb, pine needle powder, dog tail grass, gingko leaf and water. The preparation of the fertilizer comprises mixing the components, stacking to ferment, crushing, stirring, granulating, drying, cooling, sieving, weighing and packaging.    USE - Used as dairy manure organic fertilizer.    ADVANTAGE - The fertilizer: improves soil; retains water and nutrients; supplements crop organic nutrients and trace elements required for growth; and degrades residues of pesticides and fertilizers in soil.    DETAILED DESCRIPTION - Dairy manure organic fertilizer comprises 600 kg fresh cow dung, 300 kg humic acid, 100 kg bentonite, 50 kg dry powder of turtle shell, 50 kg rhizoma imperatae, 40 kg cockscomb, 100 kg wood shaving, 60 kg lotus leaf, 50 kg suberect spatholobus stem, 30 kg pepper, 20 kg seed of cowherb, 20 kg pine needle powder, 30 kg dog tail grass, 50 kg gingko leaf and 200 kg water. The preparation of the fertilizer comprises mixing the components, stacking to ferment for 3-4 days at 50-60 degrees C, crushing, stirring, granulating, drying until the water content is less than 4%, cooling, sieving to remove particles having diameter of more than 5 mm, sieving to remove particles having a diameter of less than 1 mm, weighing and packaging. An INDEPENDENT CLAIM is also included for a device to prepare the fertilizer, comprising sequentially set turner, fermentation tank, semi wet crusher, a stirrer, a granulator, a drying machine, a cooling machine, a sieving machine, a secondary sieving machine, a coating machine and a packaging steelyard. The fermentation tank has an upper rubber shed, which has a hot air furnace, a hot air dryer, and dust remover.
NOVELTY - Preparing nutrient soil involves adjusting water content of a pot, dissolving urea in water, mixing fermentation agent and rice bran, adding sawdust to rice bran mixture, spraying urea solution on mixture, piling sawdust mixture, fermenting mixture by covering pile using a plastic film, turning the mixture, adding meadow soil, burnt soil, plant ash, vermiculite, perlite, bone meal, and manure, to sawdust soil, mixing evenly, and allowing mixture to stand, and (f) stirring mixture by placing in an iron stove.    USE - The method is useful for preparing nutrient soil for culturing Cinnamomum camphora (claimed).    ADVANTAGE - The prepared soil increases survival rate of C.camphora.    DETAILED DESCRIPTION - Preparing nutrient soil involves (a) adjusting water content of a pot to 65-70%, and dissolving urea in water to obtain a urea solution, (b) mixing fermentation agent and rice bran to obtain rice bran mixture, (c) adding sawdust to rice bran mixture, spraying urea solution on the mixture, and stirring the mixture for 15-20 minutes to obtain a sawdust mixture, (d) piling the sawdust mixture, fermenting the mixture by covering the pile using a plastic film, turning the mixture after temperature reaches 70 degrees C, turning the mixture again after temperature reaches 70 degrees C, and fermenting the mixture for 20 days to obtain sawdust soil, (e) adding meadow soil, burnt soil, plant ash, vermiculite, perlite, bone meal, and manure, to sawdust soil, mixing evenly, and allowing the mixture to stand for 1 day, and (f) stirring the mixture by placing in an iron stove.
NOVELTY - Use method of Spartina alterniflora resources, comprises (i) harvesting Spartina alterniflora, pre-processing, and carrying out steam fermentation, and subjecting to desalting treatment; (ii) preparing culture medium by mixing the processed material with wheat bran, corn flour and activated carbon, and composting to ferment; and (iii) culturing yellow mushroom by inoculating strain into the culture medium.    USE - The method is useful in use method of Spartina alterniflora resources (claimed).    ADVANTAGE - The method achieves complete utilization of Spartina alterniflora resources; produces harmless chemical substances; and is economical, and environmental friendly.
NOVELTY - Traditional Chinese medicinal oral liquid comprises 6-12 pts. wt. Gentiana, 6-10 pts. wt. Phellodendron, 4-9 pts. wt. dyer's woad leaf, 4-9 pts. wt. cogongrass rhizome, 4-9 pts. wt. Sanguisorba officinalis, 4-8 pts. wt. self-heal, 3-6 pts. wt. rhizoma anemarrhenae and 2-5 pts. wt. myrobalan.    USE - The traditional Chinese medicinal oral liquid is useful for treating bovine viral diarrhea (claimed).    ADVANTAGE - The oral liquid is nontoxic and causes no side effects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the oral liquid, which involves (a) weighing the above-mentioned raw materials, adding 10 times of water, extracting mixture for 2 hours, and filtering mixture to obtain extract (I) and residue, (b) adding 10 times of water to residue, extracting mixture for 1.5 hours, and filtering mixture to obtain extract (II), (c) mixing extracts (I) and (II), and concentrating filtrate at 70 degrees C to a relative density of 1.1-1.15, (d) adding ethanol to concentrated filtrate, until the ethanol content reaches 70%, allowing mixture to stand for 12 hours, filtering mixture, recovering ethanol, and concentrating filtrate at 70 degrees C to a relative density of 1.17-1.22, and (e) mixing concentrated filtrate with water, mixing uniformly, refrigerating mixture for 48 hours, adding sodium benzoate, mixing uniformly, filling, and sterilizing the product.
NOVELTY - Polydopamine-modified reduced graphene oxide comprises reduced graphene oxide and polydopamine which is physically adsorbed to the surface of reduced graphene oxide.    USE - Polydopamine-modified reduced graphene oxide is used in photoacoustic ultrasound multimodal imaging or in preparation of photothermal cancer therapy applications (all claimed).    ADVANTAGE - The polydopamine-modified reduced graphene oxide can be mass-produced by a simple and environment-friendly method at low reduction temperature, without using a stabilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of polydopamine-modified reduced graphene oxide, which involves completely dissolving graphene oxide and dopine hydrochloride in a mass ratio of (1-4):(1-4) in a solvent to obtain a mixed solution, adjusting the pH of mixed solution to 8.5-9, and reacting at 55-65 degrees C for 12-24 hours.
NOVELTY - Treatment of involves processing fresh chicken manure and auxiliary material in weight ratio of 7-8:2-3 and mixing uniformly. Dry chicken manure and water are mixed uniformly in weight ratio of 8-9:1-2. Fresh chicken manure, dry chicken manure, leavening agent, soft sugar and alcohol are mixed uniformly in weight ratio of 1-9:1-9:0.0001-0.002:0.01-0.05:0.02-0.1, and then fermentation process is performed in a rubber sealed container.    USE - Process for treating manure (claimed).    ADVANTAGE - The process for treating manure is cost-effective, and farmer itself can perform in home.
NOVELTY - Fermentation agent comprises 8x 107-9x 107 CFU/g Bacillus natto, 3x 107-4x 107 CFU/g B.pumilus, 3x 107-4x 107 CFU/g B.laterosporus, 700-750 U/g amylase, 100-150 U/g protease, 200-250 U/g alpha -galactosidase, 200-250 U/g mannanase, 0.8-0.85 %mass sodium carbonate, 0.2-0.25 %mass ammonium oxalate monohydrate, and 0.1-0.15 %mass citric acid monohydrate.    USE - The fermentation agent is useful for increasing mortality rate of Ascaris eggs in pig manure (claimed).    ADVANTAGE - The fermentation agent is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of increasing mortality rate of Ascaris eggs in pig manure, which involves mixing 0.5% above-mentioned fermentation agent and pig manure in ratio of 7:3, and carrying out aerobic fermentation of the mixture.
NOVELTY - Preparing organic matrix involves utilizing 30-36 part human fecaluria, 30-35 parts cotton seed hulls, 30-50 parts wheat straw stick, 30-50 parts pumpkin seedling, 10-12 parts sawdust, 10-12 parts perlite and 3-5 parts ceramic compound. 2-4% Organic fertilizer is added in the raw materials to perform fermentation at 60-70 degrees C in a rubber sealed container. 65-70 % Water and 30-35% carbon:nitrogen ratio are added in the rubber sealed container for 4 days, and then 0.90-1% extracellular matrix is added to regulate the mixture pH value at 6.5-7.05.    USE - Method for preparing organic matrix used for common Andrographis herb (claimed).    ADVANTAGE - The method enables to prepared organic matrix that increases quality and yield of common Andrographis herb.    DETAILED DESCRIPTION - Preparing organic matrix involves utilizing 30-36 part human fecaluria, 30-35 parts cotton seed hulls, 30-50 parts wheat straw stick, 30-50 parts pumpkin seedling, 10-12 parts sawdust, 10-12 parts perlite and 3-5 parts ceramic compound. 2-4% Organic fertilizer is added in the raw materials to perform fermentation at 60-70 degrees C in a rubber sealed container. 65-70 % Water and 30-35% carbon:nitrogen ratio are added in the rubber sealed container for 4 days, and then 0.90-1% extracellular matrix is added to regulate the mixture pH value at 6.5-7.05. The fermented product is dried, pulverized and granulated to obtain granules with particles size less than 10mm, and then 2-4% Bacillus subtilis and Bacillus megaterium are mixed and packaged.
NOVELTY - Method for producing seedling matrix involves (a) stacking furfural fermentation waste residue, adding urea for adjusting carbon nitrogen ratio to 25:1, and fermenting mixture, where fermentation temperature is determining depending on fermentation time and frequency of turning during fermentation, (b) exposing the fermented furfural residue to sun, and (c) weighing and mixing the fermented furfural residue with perlite, vermiculite, slag, urea, monoammonium phosphate, potassium sulfate and carbendazim.    USE - The method is useful for producing seedling matrix (claimed).    ADVANTAGE - The method produces seedling matrix with unique raw material (furfural fermentation waste residue), which saves cost, prevents diseases, shortens growth period, is not affected climatic change, enables soilless cultivation at high yield, produces agricultural product with good flavor and quality, and enables convenient management.
NOVELTY - Preparing medicinal fertilizer involves crushing 10-15 parts cane straw into powder that is mixed with 20-25 parts chicken manure, 5-10 parts sugar and 5-8 parts bone powder to obtain organic material. The organic material is fermented with 1-2 parts of bacteria to obtain fermentation product that is mixed with 10-15 parts amino acid, 15-20 parts urea, 8-10 parts potassium chloride, 1-2 parts boron fertilizer, 1-2 parts stress resistance substance and 1 parts adhesive to obtain mixture that is dried and crushed. The crushed material is pelletized, dried and packaged.    USE - Method for preparing medicinal fertilizer used for preventing and treating wampee anthracnose disease(claimed).    ADVANTAGE - The method enables to prepare medicinal fertilizer that promotes wampee growth, and ensures increased plant yield, immunity and stress resistance ability without polluting environment and leaving residue.
NOVELTY - Compound fertilizer is prepared using 40-50 pts. wt. compost made from crop straw, 15-17 pts. wt. calcium superphosphate, 32-34 pts. wt. zinc sulfate, 5-7 pts. wt. boric acid, 6-8 pts. wt. adhesive, 2-4 pts. wt. ferrous sulfate, and 1-3 pts. wt. synergist.    USE - The compound fertilizer is useful for growing cotton seedlings (claimed).    ADVANTAGE - The compound fertilizer ensure to improve crop quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the compound fertilizer, which involves (a) dissolving the above-mentioned raw materials by adding 2 times water, (b) subjecting the dissolved mixture to dry granulation, and (c) sieving the resulting granules using 100 mesh sieve to obtain product.
NOVELTY - Liquid fertilizer comprises cobalt 60 irradiated humic acid (60g/l), microorganism preparation (40 ml/l) and pyroligneous acid (1000 ml/l). Microorganism preparation is prepared by fixing of actinomycetes and silicate solubilising bacteria, and then performing fermentation to obtain fermentation product.    USE - Liquid fertilizer used for greenhouse (claimed).    ADVANTAGE - The liquid fertilizer reduces fertilizer dosage by 80%, and enhances cultivation of crop yield by 10-20%.
NOVELTY - Fertilizer composition for corn comprises Bacillus megaterium (CGMCC NO: 9489).    USE - As fertilizer composition for corn.    ADVANTAGE - The composition reduces corn ear bald tip rate, and increases corn kernels per row, grain number and grain weight.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the B.megaterium in preparation of fertilizer, where the fertilizer is prepared by mixing 65-85% fertilizer, 5-15% potassium humate, and 10-20% urea, inoculating B.megaterium and B.mucilaginosus to the mixture, and adding peat soil to the mixture.
NOVELTY - Fertilizer composition comprises 70-75 pts. wt. organic fertilizer, 4.5-5.0 pts. wt. urea, 2.5-3.0 pts. wt. calcium superphosphate fertilizer, 5.5-6.0 pts. wt. potassium fertilizer, 5-8 pts. wt. attapulgite, 1-1.5 pts. wt. rice straw decomposing agents and 1-1.5 pts. wt. potassium releasing agents.    USE - Fertilizer composition used for cultivating cabbage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing rice straw decomposing agents and potassium releasing agents with stirring, and then fermenting them for 25-30 days;    (B) adding attapulgite, urea, calcium superphosphate fertilizer and potassium fertilizer to the obtained material, and then crushing them; and    (C) granulating the obtained material to obtain the finished product.
NOVELTY - Preparing fertilizer for tobacco involves (a) mixing urea, ammonium nitrate, calcium superphosphate, potassium chloride, diammonium phosphate, magnesium sulfate, ferrous sulfate, copper sulfate, and suitable amount of water, and heating the mixture to obtain a mixed solution, (b) adding organic substance, soil conditioner, effective microorganism (EM) into the mixed solution, and fermenting the mixture, (c) drying the fermented material, and crushing the dried material, and (d) granulating the crushed material to obtain granular fertilizer.    USE - The method is useful for preparing fertilizer for tobacco (claimed).    ADVANTAGE - The prepared fertilizer provides high organic substance and nutrients to soil, and does not cause soil compaction.    DETAILED DESCRIPTION - Preparing fertilizer for tobacco involves (a) mixing 15-20 parts urea, 8-12 parts ammonium nitrate, 5-8 parts calcium superphosphate, 10-20 parts potassium chloride, 5-10 parts diammonium phosphate, 1-2 parts magnesium sulfate, 1-2 parts ferrous sulfate, 1-2 parts copper sulfate, and suitable amount of water, and heating the mixture for 20 minutes to obtain a mixed solution, (b) adding 40-50 parts organic substance, 1-3 parts soil conditioner, 1-3 parts effective microorganism (EM) into the mixed solution, and fermenting the mixture under normal conditions for 30-40 days, (c) drying the fermented material, and crushing the dried material, and (d) granulating the crushed material to obtain granular fertilizer.
NOVELTY - Nutritional soilless cultivation matrix comprises organic fertilizer, inorganic fertilizer and water retention agent. Organic fertilizer comprises 50-75 pts. wt. organic cultivation matrix, 0-50 pts. wt. cassava residue and 0-35 pts. wt. vermiculite powder. Inorganic fertilizer comprises 0.50-2.00kg urea, 0.0.15-0.60kg phosphorus pentoxide and 0.75-3.02 kg potassium oxide. Water retention agent is mixed with organic cultivation matrix, and then inorganic fertilizer and cassava residue and vermiculite powder are mixed.    USE - Nutritional soilless cultivation matrix used for cultivating eggplant (claimed).    ADVANTAGE - The nutritional soilless cultivation matrix is eco-friendly, absorbs urea and nitrogen fertilizer needed for plant growth, and reduces loss of nitrogen fertilizer.
NOVELTY - 7-aminocephalosporanic acid (7-ACA) from 7-ACA mother liquid is recovered by adjusting 7-ACA mother liquid pH to 7 with alkali, concentrating 4-5 times, controlling temperature at 5-10 degrees C, absorbing concentrated 7-ACA mother liquid using LXT-032 resin (RTM: Lightly crosslinked thermoset resin), analyzing, adding acid to material liquid, crystallizing, filtering crystal, washing, and drying.    USE - Recovery of 7-aminocephalosporanic acid for cefotaxime, cefuroxime, cefoperazone, ceftriaxone, cefazolin, and cefepime.    ADVANTAGE - The process is scientific, reasonable, energy-saving, and environment-friendly, and has low cost and high yield and product purity.
NOVELTY - Extracting orange peel plant dye comprises naturally drying orange peel, soaking in deionized water with a bath ratio of 1:10-15, adding sodium bicarbonate to adjust the pH to 7-9, heating to 80-100 degrees C for 60-90 minutes, cooling, filtering to remove residues and drying.    USE - The method is useful for extracting orange peel plant dye (claimed).    ADVANTAGE - The method: does not add any toxic chemicals; comprises natural plant pigment; is environmentally friendly; and generates residue, which can be naturally degraded and can be used as a natural fertilizer after treatment, which does not cause environmental pollution.
NOVELTY - The luminescent material includes nano level hexagonal disk-shaped fluoride (I).    USE - Luminescent material used in storage transmission, optical display applications, infrared detection, fluorescent security, fluorescent probes, biosensors and biological imaging (claimed).    ADVANTAGE - The luminescent material ensures excellent light-emitting efficiency.    DETAILED DESCRIPTION - The luminescent material includes nano level hexagonal disk-shaped fluoride of general formula NaLu1-x-y-xRxY'byM2F4 (I).    R=rare earth element yttrium;    Y'=gadolinium or lanthanum;    M=rare earth element holmium, thulium or erbium; and    x,y and z=0-0.1.    An INDEPENDENT CLAIM is included for a method for preparing luminescent material, which involves:    (A) weighing the raw material according to stoichiometric ratio of the elements;    (B) adding the weighed material in a three-necked flask with oleic acid and octadecene under nitrogen gas or an inert gas conditions at 140-180 degrees C for 30-60 minutes to form a solution;    (C) dissolving ammonium and sodium hydroxide in methanol to obtain another solution;    (D) injecting the former solution into the latter solution at 40-60 degrees C for 30-60 minutes for evaporating methanol to obtain solution;    (E) heating the formed solution under nitrogen gas or an inert gas conditions at 300-330 degrees C for 1-3 hours;    (F) cooling the formed solution at room temperature to form nanocrystalline; and    (G) centrifuging the formed nanocrystallines with an excess of anhydrous ethanol to get the luminescent material.
NOVELTY - Producing mannan oligosaccharide (MOS) by either: hydrolyzing konjak flour using beta -mannase from laboratory autonomous constructed Pichia pastoris recombinant GS115/Auman26A; or enzymatic combined ultra-filtration process, comprising determining hydrolysis rate index of konjak flour substrate, determining hydrolysis conditions through single factor test, optimizing enzymolysis by using 60 U enzyme/g konjak flour, enzymolysis, completing the reaction by inactivating enzyme, cooling, centrifuging hydrolyzate, filtering via ultrafiltration device, is claimed.    USE - The method is useful for producing mannan oligosaccharide by hydrolyzing konjak flour using beta-mannase from laboratory autonomous constructed Pichia pastoris recombinant GS115/Auman26A (claimed).    ADVANTAGE - The method: utilizes enzyme, which has high catalytic activity and low production rate; is short, environmentally friendly and economical; has simple purification and separation steps; lays a foundation to produce refined low-polymerized mannan oligosaccharide; and is suitable for large scale industrial production.    DETAILED DESCRIPTION - Producing mannan oligosaccharide (MOS) by either: hydrolyzing konjak flour using beta -mannase from laboratory autonomous constructed Pichia pastoris recombinant GS115/Auman26A; or enzymatic combined ultra-filtration process, comprising determining hydrolysis rate index of konjak flour substrate, determining hydrolysis conditions through single factor test, optimizing enzymolysis by using 60 U enzyme/g konjak flour, enzymolysis at 40 degrees C for 5 hours, where the konjac flour content is 30 g/l, completing the reaction by inactivating enzyme in boiling water, cooling, centrifuging the enzyme hydrolyzate, filtering via 0.45 mu m membrane ultrafiltration device having a molecular weight cutoff value of 2000 kDa, preferably less than 2000 at 0.2 MPa, is claimed.
NOVELTY - The system has photovoltaic cells (2) connected to a hydrogen plant. A connecting pipe (4) provided with a circulation pump (3). A hot water storage tank (5) is provided with a water supplement tank (7). A hydrogen producing device (9) is provided with the water supplement tank. A hydrogen outlet pipe (13) is provided with an oxygen storage cabinet (15). The photovoltaic cell is connected with the hydrogen producing device.    USE - Solar hydrogen hot water supply system.    ADVANTAGE - The system improves overall efficiency of solar energy utilization. The system is better in a sunlight area for preparing solar energy hot water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a solar hydrogen hot water supply system.    Photovoltaic cells (2)    Circulation pump (3)    Connecting pipe (4)    Hot water storage tank (5)    Water supplement tank (7)    Hydrogen producing device (9)    Hydrogen outlet pipe (13)    Oxygen storage cabinet (15)
NOVELTY - Forming a catalyst system comprises (a) combining one or more compounds comprising an element including alkaline earth element X and a metal element Y; (b) mixing the one or more compounds to form a mixture; and (c) calcining the mixture to form a catalyst system. The alkaline earth element X is magnesium, calcium, beryllium and/or barium. The metal element Y is aluminum, manganese, iron, cobalt, nickel, chromium, gallium, boron, lanthanum, phosphorus, titanium and/or zinc.    USE - The catalyst system is useful in catalytic pyrolysis process or gasifiction of solid biomass material.    DETAILED DESCRIPTION - Forming a catalyst system comprises (a) combining one or more compounds comprising an element including alkaline earth element X and a metal element Y; and either (b) mixing the one or more compounds to form a mixture; and (c) calcining the mixture to form a catalyst system; or precipitating the compounds to form the catalyst system. The alkaline earth element X is magnesium, calcium, beryllium and/or barium. The metal element Y is aluminum, manganese, iron, cobalt, nickel, chromium, gallium, boron, lanthanum, phosphorus, titanium and/or zinc. The catalyst system comprises a composition represented as (X1O).(X2O)a.(X3YbO4).    X1 , X2 and X3 = alkaline earth elements comprising Mg, Ca, Be and/or Ba;    a = 0 or 1; and    b = 0.1 or 2.    An INDEPENDENT CLAIM is also included for a method (ii) of forming a catalyst system, comprising calcining an anionic or cationic clay comprising at least one alkaline earth element and aluminum at 900 degrees C.
NOVELTY - Fermenting animal stool tower, relating to cultivation livestock and poultry excrement treatment device. Set with pedestal, a feed box, operation guide plate, operation pull rod, a handle, a pulling plate and turning plate; provided with at least 2 layer up a box pedestal, a material tank set with vent hole, provided with a base in between adjacent material tank, provided with a base between at most low box and pedestal, provided with a component, a component operation by pulling pole and operation handle one between a base and a material tank, one operation end pulling pole and a pulling plate is connected, setting b box upper part of reverse turning bed through operation guide plate and a connection plate, a component through rotating and a pulling plate connected to a reverse turning bed is a livestock excrement by the upper layer to bottom layer material feed tank, between the operation plate and a base provided with a base, provided with protecting awning at the upper most box. One-off inoculation, does not need repeated inoculation. Operation is simple, it saves force and strong practicability.
NOVELTY - Cultivating green beans comprises: selecting a deep soil layer land having rich organic matter content; deeply plowing the land, raking thin soil to form high bed deep groove having 1.5 m deep and 1 m wide, then administering base fertilizer between the trenches; selecting large grain, full, insect disease-free seeds, disinfecting the seeds with 50% carbendazim before sowing, then sowing 3-4 grains into each groove; carrying out first weeding after 10 days of sowing, clearing the groove soil to promote adventitious root; and spraying chlorothalonil powder to e.g. control leaf spot disease.    USE - The method is useful for cultivating green beans (claimed).    ADVANTAGE - The fertilizer increases the yield and quality of fruit with increased vitamin and mineral content.    DETAILED DESCRIPTION - Cultivating green beans comprises: (i) selecting a deep soil layer land having rich organic matter content, loose, fertile, good drainage and sand loam pH of 6-7; (ii) deeply plowing the land, raking thin soil to form high bed deep groove having 1.5 m deep and 1 m wide, then administering base fertilizer between the trenches, where the base fertilizer comprises 560-600 kg/acre dry chicken manure, 120-150 kg/acre straw ash, 320-380 kg/acre slow-release granule fertilizer and 100-140 kg/acre soil conditioner; (iii) selecting large grain, full, insect disease-free seeds, disinfecting the seeds with 50% carbendazim before sowing, then sowing 3-4 grains into each groove for 2 rows having 65-70 cm deep and a distance of 25-30 cm away from each groove; (iv) carrying out first weeding after 10 days of sowing, then second weeding before climbing vine, clearing the groove soil of the plant stem base to promote adventitious root; and (v) alternately spraying chlorothalonil powder to control leaf spot, rust disease, powdery mildew and anthracnose in green beans.
NOVELTY - A cobalt diselenide modified carbon fiber composite material comprises cobalt diselenide nanoribbons supported on surface of carbon fiber felt.    USE - Cobalt diselenide modified carbon fiber composite material used for catalyst of electric water analysis hydrogen catalytic reaction (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cobalt diselenide modified carbon fiber composite material comprising mixing diethylenetriamine and water at volume ratio of 2:1, dissolving cobalt acetate and sodium selenite, adding carbon fiber felt, ultrasonically cleaning, transferring into hydrothermal reaction kettle, sealing, drying at 150-200 degrees C for 12-18 hours, taking out, cooling to room temperature, washing with ethanol, washing and vacuum-drying.
NOVELTY - This utility new type provide the a one organic fertilizer stacking, relating to a composting is characteristic of fertilizer preparation field, this stack turning machine comprises a machine frame guide rail, a wheel, a rotating shaft, a turning motor, a straight pole, a turning claw, a detachable sleeve, a pole, a bracket, a cleaning plate, machine cover, equal pressure sensor component, a work component mounted in the sleeve structure is a detachable changing up, at the same time a height adjustable sleeve so as to control stirring blade extends into the depth of fertilizer, increase the application range of dumper reducing the production a multi-source organic fertilizer raw material is a cost, and a turning automatic degree and turning efficiency, single turning in solving the technology is suitable for range is small, at the same time can only be fixed over a horizontal plane of fertilizer, working efficiency is low, turning depth equal small problem.
NOVELTY - The method involves fine-crushing organic waste (2) in a wet bead mill (4). The finely-crushed organic waste (5) is fed into a methane fermentation tank (6) and is decomposed and fermented by anaerobic microbes, generating methane gas (3). The digestive liquid (7) resulting from fermentation is separated into a concentrate (15) and permeate (16) by an ultra-filtration membrane (8). The concentrate is returned to the fermentation tank. The contents of the tank are stirred by water flow arising from return of concentrate.    USE - Fermentation method for methane.    ADVANTAGE - Since the organic wastes are finely crushed prior to fermentation, decomposition of the finely crushed wastes by anaerobic microbe is easily advanced, enabling efficient methane gas production. The pores of the ultra-filtration membrane are hardly clogged, enabling to easily separate digestive liquid into concentrate and permeate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methane fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a methane fermentation system. (Drawing includes non-English language text).    Organic waste (2)    Methane gas (3)    Wet bead mill (4)    Finely-crushed organic waste (5)    Methane fermentation tank (6)    Digestive liquid (7)    Ultra-filtration membrane (8)    Concentrate (15)    Permeate (16)
NOVELTY - Simultaneous acceleration of Sclerotinia sclerotiorum and crop straw decomposition comprises spraying with 15 g/acre composite microbial agent aqueous solution containing composite agent and water at weight to volume ratio of 15:15, harvesting, standing for 3-5 days and applying complex microbial fertilizer at an amount of 10 kg/acre.    USE - Method for carrying out simultaneous acceleration of Sclerotinia sclerotiorum and crop straw decomposition (claimed).    ADVANTAGE - The method is labor-saving, time-saving and low-cost and effectively increases crop yield.
NOVELTY - Compound fertilizer comprises 2-4 pts. wt. urea, 5-7 pts. wt. potassium chloride, 2-5 pts. wt. zinc sulfate, 3-7 pts. wt. borax, 4-6 pts. wt. ammonium phosphate fertilizer as biogas manure and 1-3 pts. wt. ammonium citrate.    USE - Compound fertilizer used for cultivating peanut (claimed).    ADVANTAGE - The compound fertilizer is prepared in simple manner by requiring waste materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound fertilizer, which involves drying, crushing, mixing and sieving raw materials.
NOVELTY - Biofertilizer comprises 5-55 pts. wt. coal gangue granules, 5-50 pts. wt. peat, 1-30 pts. wt. coal ash, 5-15 pts. wt. pond sludge, 30-75 pts. wt. plant ash, 20-30 pts. wt. straw, 15-55 pts. wt. livestock and poultry excrement and 0.1-15 pts. wt. micro-organism powder.    USE - Biofertilizer used for restraining soil-borne diseases.    ADVANTAGE - The biofertilizer is prepared in a simple manner, and cost-effective and eco-friendly, and improves quality and structure of soil, and has wide industrial applicability.
NOVELTY - Preparing flower nutrient soil involves drying, crushing and mixing straw, wood chips leaves waste, animal waste and microbial fermentation additives. The obtained mixture is fermented at 30-40 degrees C for 10-20 days to obtain lignocellulosic waste material. The medical stone is washed, dried and crushed to obtain medical stone powder. Fermented lignocellulosic material, river mud, attapulgite clay, medical stone powder, wood meal and perlite powder are mixed, dried and screened to obtain product.    USE - Method for preparing flower nutrient soil used for preserving moisture (claimed).
NOVELTY - Soil-less matrix comprises organic mixture, grass peat, perlite, vermiculite, plant ash and inorganic fertilizer.    USE - Soil-less matrix used for cultivating tomato seedling (claimed).    ADVANTAGE - The soil-less matrix is economic, and reduces harmful waste matter.
NOVELTY - Fertilizer is prepared by grinding basalt stone through 300 meshes and then natural microporous minerals elements are mixed. Bacillus subtilis (1%) is mixed with the product to perform fermentation process.    USE - Fertilizer used for eutrophication of soil to regain its vitality and for making oxygen-enriched ecology (claimed).    ADVANTAGE - The fertilizer prevents damage of soil caused by pesticide, and restores productivity of the soil.
NOVELTY - Nutritional fertilizer comprises base fertilizer and inorganic compound fertilizer. Base fertilizer comprises 60-75 pts. wt. oil cake, 5-10 pts. wt. bagasse pith, 0.5-2 pts. wt. Bacillus subtilis, 0.5-2 pts. wt. thermophilic spore, 10-15 pts. wt. potassium humate, 10-12 pts. wt. potassium magnesium sulfate and 27-41 pts. wt. water. Inorganic compound fertilizer comprises 1-4 pts. wt. Bacillus pumilus, 5-10 pts. wt. amino acid, 5-15 pts. wt. potassium nitrate, 10-20 pts. wt. potassium sulfate, 2.5-5 pts. wt. borax and 1.25-2.5 pts. wt. zinc sulfate.    USE - Nutritional fertilizer used for mammoth gold tobacco and safflower (claimed).    ADVANTAGE - The nutritional fertilizer activates soil microorganism, and nitrogen, phosphorus, potassium and nutritional elements are easily absorbed by crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutritional fertilizer, which involves:    (A) putting oil cake and bagasse pith in a fermentation pool and adding water, thermophilic spore and Bacillus subtilis to carry out fermentation at 40-60 degrees C for 20-30 days by using a device;    (B) performing fermentation of oil cake by supplying oxygen supply for 10-18 months to obtain fermented cake oil; and    (C) adding remaining components with fermented product, crushing and sieving it, and then pilletizing by using a pelleting device to obtain final product.
NOVELTY - The method involves comprising 16-19 wt.% gluey film, 4-6 wt.% andong alcoholic meal, 2.5-3.5 wt.% saccharomyces cerevisiae, 10-12 wt.% soymilk residue, 4-6 wt.% apple pomace and 0.85-1.2 wt.% culture fluid. A main raw material measuring process is performed (S100) to measure a main raw material. A high-temperature sterilization process of the film is performed (S200). Atmosphere fermentation process of the material is performed (S300) by probviding the film in a fermenter. Anaerobic fermentation process of the material is processed (S400) by providing the fluid in the fermenter.    USE - Method for manufacturing main raw material of a livestock in a stockbreeding farmhouse.    ADVANTAGE - The method enables reducing manufacturing cost and avoiding economical charge of stockbreeding farmhouse. The method enables simplifying manufacturing process of a high quality fodder. The method enables presenting optimal fermentation circumstance in the main raw material, so that productivity of the main raw material is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing main raw material of a livestock.'(Drawing includes non-English language text)'    Step for performing a main raw material measuring process (S100)    Step for performing high-temperature sterilization process of gluey film (S200)    Step for performing atmosphere fermentation process of a main raw material (S300)    Step for processing anaerobic fermentation process of a main raw material (S400)
NOVELTY - The manhole has an open channel (12) that connects the line rear portion of an inverter of a oval linear portion and an inverter (11) that is formed in either of the side of the lower portion. A womanlike face portion (20) charges the filter media (21) to a fitting structure in open channel and sets up a ware (30) for speed of current increase in inverter central portion of position of open channel water exit. A bio-filter is formed in the portion of sewage that is flowed into inverter that is branched to an open channel and flows in contact with filter media.    USE - Manhole for use in sewage disposal plant or sewer system.    ADVANTAGE - The water quality is improved. The base decomposition effect is provided effectively. The carrying capacity at the inverter is not obstructed. The sewage and wastewater treatment rate are improved by the continuous decomposition of the substrate. The flow including the suspended solids is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the manhole.    Inverter (11)    Open channel (12)    Womanlike face portion (20)    Filter media (21)    Ware (30)
NOVELTY - Method of cultivating goose, involves selecting good quality water source, feeding goose for 12 hours, where the feed comprises Chinese herbal medicine and 60 wt.% corn flour, 14 wt.% wheat bran, 10 wt.% rice bran, 11 wt.% vegetable cake, 3.7 wt.% fish meal, 1 wt.% piglet bone powder and 0.3 wt.% edible salt, then injecting goose with plague antibody and disinfecting periodically with 2% formalin or 20% lime water.    USE - The method is useful for cultivating goose (claimed).    ADVANTAGE - The method is rapid, cost-effective and environmentally-friendly. The feed does not contain any pigment and hormone, and enhances disease resistance and promotes appetite of goose.
NOVELTY - This utility new type claims a a pig farm dung and fertilizer comprehensive use system, belongs to industry waste treatment field, the device comprises primary settling sedimentation pool, regulating pool fertilizer, material pump, water pump, pH monitoring device, pH neutralizing device and medicine-adding device, primary settling pool is z mother pool structure, comprising subloop, , z a solid-liquid mixing discharging pool wherein, and material pump, the upper has set liquid outlet, through water pump and sedimentation pool connected, in sedimentation pool. has a pH monitoring device and a pH neutralizing, sedimentation pool through water pump and the fertilizer regulating pool connected, in the fertilizer regulating pool set with medicine adding device, the utility model is new type using z mother pool for sedimentation principle carry out solid-liquid separating process, and using absorbing, filtering and biological fermentation self-purification, the pig is a high concentration waste liquid carrying out rapid purification is discharged, and is made of organic fertilizer, at the same time, process is simple, the cost is low, effective solves the problem of a large scale and pig waste liquid pollute.
NOVELTY - A composting kitchen waste deodorization complex conditioner comprises crop straw, pulverized coal ash and potassium carbonate at mass ratio of (10-20):(1-2):(2-3).    USE - Composting kitchen waste deodorization complex conditioner.    ADVANTAGE - The method is simple and easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process of kitchen waste composting deodorizing method comprising taking 10-20:80-90 mass ratio of composting kitchen waste deodorization complex conditioner and kitchen waste, mixing, and composting for 20-30 days via oxygen continuous air method at air quantity of 0.15-0.25 m3/hour.
NOVELTY - A yew fertilizer is prepared by taking 42.2-46.5 wt.% fir slag, 35.0-37.5 wt.% mud material, 14.2-17.5 wt.% fir leaf powder and 3.1-3.5 wt.% biological activity degradation agent, mixing, stirring, pile stacking, fermenting for 62-87 days, stirring, and packing.    USE - Method for preparing yew fertilizer (claimed).
NOVELTY - A mixed waste fertilizer comprises 40-60 pts. wt. sodium alginate, 20-25 pts. wt. slaughterhouse waste animal viscera, 60-80 pts. wt. fermented rice, 14-22 pts. wt. microzyme, 60-80 pts. wt. weed and 8-10 pts. wt. vitamin B6.    USE - Mixed waste fertilizer.    ADVANTAGE - The fertilizer promotes rapid plant growth.
NOVELTY - A compound fertilizer comprises Azotobacter powder, sweet potato powder, peat, calcium superphosphate, Bacillus sphaericus powder, rice straw, polyvinylidene potassium phosphate, ammonium dihydrogen phosphate, silicate bacteria, Bacillus cereus, semen litchi core, shelled semen biotae, Bacillus thuringiensis, chicken manure, and wheat bran.    USE - Compound fertilizer used for improving soil (claimed).    ADVANTAGE - The fertilizer is efficient, has long acting effect, increases quality of crops, restrains soil-borne disease, and has low cost and no residue and pollution.    DETAILED DESCRIPTION - A compound fertilizer comprises 0.01-0.02 pt. wt. Azotobacter powder, 21-30 pts. wt. sweet potato powder, 45-50 pts. wt. peat, 9-16 pts. wt. calcium superphosphate, 0.01-0.02 pt. wt. Bacillus sphaericus powder, 40-50 pts. wt. rice straw, 3-7 pts. wt. polyvinylidene potassium phosphate, 8-13 pts. wt. ammonium dihydrogen phosphate, 0.01-0.02 pt. wt. silicate bacteria, 0.03-0.07 pt. wt. Bacillus cereus, 6-7 pts. wt. semen litchi core, 3-5 pts. wt. shelled semen biotae, 0.001-0.002 pt. wt. Bacillus thuringiensis, 20-25 pts. wt. chicken manure, and 16-26 pts. wt. wheat bran.
NOVELTY - A sugarcane fertilizer comprises 100-150 pts. wt. sludge, 80-100 pts. wt. sugarcane leaves, 40-60 pts. wt. stool, 200-250 pts. wt. urea, 10-30 pts. wt. humic acid, 50-80 pts. wt. ammonium nitrate, 20-30 pts. wt. potassium chloride, 50-80 pts. wt. potassium sulfate, 5-8 pts. wt. magnesium sulfate, and 50-80 pts. wt. calcium superphosphate.    USE - Sugarcane fertilizer.    ADVANTAGE - The fertilizer can promote efficient use of nitrogen, phosphorus and other nutrients, reduces soil nitrogen and phosphorus accumulation and loss, and prevents soil pollution.
NOVELTY - Microorganism compound fertilizer comprises 0.01-0.03 pt. wt. abamectin mixture, 12-19 pts. wt. ammonium dihydrogen phosphate, 15-25 pts. wt. calcium phosphate, 5-9 pts. wt. potassium dihydrogen phosphate, 9-14 pts. wt. stone powder, 5-6 pts. wt. coco peat powder, 1-2 pts. wt. Psidium guajava leaves, 3-6 pts. wt. calcite, 4-10 pts. wt. Chimonanthus praecox, 1-2 pts. wt. Milan sawdust, 3-9 pts. wt. Murraya paniculata sawdust, 2-8 pts. wt. dipotassium hydrogenphosphate, and 1-2 pts. wt. boric acid.    USE - Microorganism compound fertilizer used for dry land crop.    ADVANTAGE - The fertilizer is non-toxic, has nitrogen, phosphorus, potash and trace elements content in crops, water retention capacity and better and longer fertilizer effect, and improves soil structure.
NOVELTY - Synthesis of 3,4-dihydropyrimidinone drug intermediate (I) comprises reacting benzyl halide (II), beta -carboxylic acid ester (II) and hydrazine derivative (III) in the presence of strontium bis(trifluoromethanesulfonate) and hydrogen peroxide at 80 degrees C.    USE - Method for synthesizing 3,4-dihydropyrimidinone drug intermediate (claimed).    ADVANTAGE - The synthesis is environment-friendly, has mild reaction conditions, high catalyst recovery and 95% product yield.    DETAILED DESCRIPTION - Synthesis of 3,4-dihydropyrimidinone drug intermediate of formula (I) comprises reacting benzyl halide of formula (II), beta -carboxylic acid ester of formula (III) and hydrazine derivative of formula (IV) in the presence of strontium bis(trifluoromethanesulfonate) and hydrogen peroxide at 80 degrees C.    X=Cl or Br; and    Y'=O or S.
NOVELTY - An F175-3 protein comprising: (a) fully defined 429 amino acids (SEQ ID NO. 2) given in the specification; and (b) amino acid sequence of (a) having one or more amino acid residues that are substituted, deleted, and/or added and comprising the same function of (a), is new.    USE - The F175-3 protein, DNA molecule, recombinant vector, recombinant bacterium, or transgenic cell line is useful for preparing cellulase or 3-glucanase, preferably endocellulase or exocellulase, where the enzyme has optimum pH value of 5.0, and optimum temperature of 60 degrees C; and for degradation of biomass, preferably corn biomass (claimed).    ADVANTAGE - The F175-3 protein can retain activity of greater than or equal to 80% or 88.5% at optimum conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a DNA molecule encoding the F175-3 protein;    (2) a recombinant vector, recombinant bacterium, and transgenic cell line comprising the DNA molecule; and    (3) a method for preparing cellulase or 3-glucosidase comprising culturing the recombinant bacteria.
NOVELTY - One a municipal resident kitchen garbage processing system, comprising kitchen garbage crushing machine, solid-liquid separating device and compost processing device, the kitchen garbage crushing machine mounted in the water of a residential kitchen sink, discharging end of kitchen garbage crushing machine and resident building sewer pipeline connection, each building residential building sewer pipeline of end has a solid-liquid separating device, a solid-liquid separating device using capsule type solid-liquid separating device, a feeding terminal further connected and household toilet discharging liquid channel, the liquid outlet end a municipal sewage pipe network, filter cake down a filter cake through a transport vehicle to deliver compost treatment device. The system use independently smashing, pressing into filter cake collection at last compost treatment is to make the collection and treatment equal link linked, can solve the collection process pollute environment, landfill or incineration disposal module cause resource waste problem equal, a kitchen garbage recycling processing.
NOVELTY - A traditional Chinese medicine composition is prepared by taking rhubarb, lily, groundsel, peach, rhizoma smilacis glabrae, wild rose, bean sprout, and Kadsura longipedunculata, crushing bean sprout and Kadsura longipedunculata, putting into carbon dioxide supercritical fluid extraction vessel, adding ethanol, extracting, mixing remaining raw materials, performing microwave extraction, combining extracts, concentrating, putting into macroporous resin column, eluting, recovering ethanol, concentrating, drying, adding starch and ethanol, pelletizing, drying, and tableting.    USE - Method for preparing traditional Chinese medicine composition used for treating and preventing lymphoid tumor cells (claimed).    DETAILED DESCRIPTION - A traditional Chinese medicine composition is prepared by taking 291 g rhubarb, 103 g lily, 92 g groundsel, 92 g peach, 92 g rhizoma smilacis glabrae, 62 g wild rose, 62 g bean sprout, and 62 g Kadsura longipedunculata, crushing bean sprout andKadsura longipedunculata into fine powder, putting into carbon dioxide supercritical fluid extraction vessel, adding 4-6% ethanol as extraction solvent, extracting at 30-60 degrees C for 130-170 minutes under 20-30 MPa pressure and carbon dioxide flow rate of 1-3 mL/g to obtain supercritical extract, standing, mixing remaining raw materials, adding 5 L 60% ethanol, performing microwave extraction twice at power of 600-800 W for 5-10 minutes, combining extracts, concentrating, putting into macroporous resin column, eluting with 60% ethanol, recovering ethanol under vacuum pressure, concentrating, drying, adding starch and 60% ethanol, pelletizing, drying, and tableting.
NOVELTY - Preparation of nanodrug-loading fiber film with temperature sensitive drug release property comprises weighing and taking poly N-isopropyl acrylamide, ethyl cellulose and anhydrous ethanol, mixing, adding drug, magnetic stirring for 24-48 hours to obtain spinning source liquid; and electrostatic spinning nanofiber film and vacuum-drying. The mass ratio of poly N-isopropyl acrylamide and ethyl cellulose is 1:1-4.    USE - Method for preparing nanodrug-loading fiber film with temperature sensitive drug release property (claimed).    ADVANTAGE - The film has analgesic property, convenient administration, simple process, no pollution and low cost. The method is easy to carry and fits large scale production.
NOVELTY - Ethanologenic yeast with xylose assimilation ability is produced by successively performing process (a) of aerobically culturing yeast belonging to Kluyveromyces genus in culture medium containing 5-30 mM of iron salt, process (b) of isolating iron tolerant mutant yeast grown in process (a), and process (c) of selecting iron tolerant mutant yeast which has concentration of greater than or equal to 1.5 times the ethanol concentration in culture medium where yeast used for culturing in process (a) is cultured for 48-72 hours.    USE - Production of ethanologenic yeast with xylose assimilation ability for ethanol production (claimed).    ADVANTAGE - Ethanol can be efficiently produced at low cost, without using gene modification technology.    DETAILED DESCRIPTION - Ethanologenic yeast with xylose assimilation ability is produced by successively performing process (a) of aerobically culturing yeast belonging to Kluyveromyces genus in culture medium containing 5-30 mM of iron salt, process (b) of isolating iron tolerant mutant yeast grown in process (a), and process (c) of selecting iron tolerant mutant yeast which has concentration of greater than or equal to 1.5 times the ethanol concentration in culture medium where yeast used for culturing in process (a) is cultured for 48-72 hours and ethanol concentration in culture medium which contains xylose as carbon source and where iron tolerant mutant yeast isolated in process (b) is cultured for 48-72 hours. An INDEPENDENT CLAIM is included for production of ethanol which involves culturing ethanologenic yeast with xylose assimilation ability in culture medium containing xylose as carbon source.
NOVELTY - The method involves sending food waste which is crushed with separation removal of foreign substance. The dehydration cake is sent to second dehydration process. The coagulant is provided to supply fiber small powder to reactant supplying lime. The effluent is supplied in preprocess phase and is sent to aerobic biological processing in certain range. A first aeration tank is connected to aeration tribute class pump. The ejected excess sludge is sent to influx container. The food waste is processed in first aerobic biological process solution.    USE - Method for processing food waste.    ADVANTAGE - The concentration of salinity and organic compound are increased. The methane fermentation and alcohol fermentation for processing food waste is performed. The water-soluble organic matter and liquid organic compound are dehydrated using lime. The pollution load for processing food waste is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the food waste disposal process map. (Drawing includes non-English language text)
NOVELTY - The method involves removing the foreign substance and supplying a dehydration cake in which the dehydration is performed to an anaerobic liquefaction tub. The acid broth is supplied to the methane fermenter and the organic compound is disassembled in 50-60 degrees C with the methane bacteria. The methane fermentation liquid of the methane fermenter for spawn is supplied. The acid fermentation is supplied to the methane fermenter and the liquid food waste is supplied to the acid fermentor. The temperature is maintained at specific value.    USE - Method for treating food waste.    ADVANTAGE - The ocean pollution is aggravated and the ocean dumping is prohibited. The composting, methane fermentation and alcohol fermentation are performed efficiently. The pollution load of the effluent is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the process for treating food waste. (Drawing includes non-English language text)
NOVELTY - Treatment of food waste involves crushing food waste, dehydrating the resultant product, providing the resultant product into high-temperature fermenter, then injecting microorganisms, fermenting the resultant product at 35-45 degrees C, carrying out liquefaction process, providing the resultant product into scrambler, adding ball-type binder or pellet-type binder, mixing the resultant product and drying.    USE - Treatment of food waste (claimed).
NOVELTY - Producing bio-methane, comprises (a) adding organic waste containing iron-based organic matter into a reactor, pressurizing by applying high-temperature steam on the reactor, and hydrolyzing the organic matter by stirring, (b) venting the steam from inner of the reactor, and crushing cell wall of hydrolyzed organic matter in low molecular weight by rapid decompressing within the reactor, and (c) adding the low molecular weight organic matter in a anaerobic fermentation tank to produce bio-methane.    USE - The bio-methane is useful in power generation system (claimed).    ADVANTAGE - The method improves production efficiencies more than 50%, improves fermentation speed of methane, removes odor substance, shortens processing time, and is economical.
NOVELTY - The method involves supplying food waste that is crushed with the separation removal of the foreign substance and providing a dehydration cake for composting process. The lime and fly ash are injected into the dehydration filtrate. The aerobic biological treatment is performed in the settling tank. The air is supplied to the lower portion of a bio-reactor in which the filler of the activated humic substance pellet and active mineral component are provided. The ejected excess sludge is sent to the influx container and deodorization process is performed.    USE - Method for processing food waste.    ADVANTAGE - The ocean pollution is aggravated and the ocean dumping is prohibited. The composting, methane fermentation and alcohol fermentation are performed efficiently. The pollution load of the effluent is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the process for processing food waste. (Drawing includes non-English language text)
NOVELTY - Method for preventing and controlling disease and insect pest during annual production of flowering cabbage, involves performing cultivation process, and performing physical control, agricultural control, biological control, and auxiliary chemical control process.    USE - The method is useful for preventing and controlling disease and insect pest during annual production of flowering cabbage (claimed).    ADVANTAGE - The method enables to prevent and control disease and insect pest in an environmentally-friendly manner, without using chemical pesticide, and with control rate of more than 90%.
NOVELTY - A town sewage denitrogenation and phosphorus-removal method involves selecting dominant algae variety identified from the municipal wastewater treatment plant as the algae source, and adopting active sludge as a bacterial source. An elastic three-dimensional filler is selected as an immobilized filler, and the sewage is treated according to an algae bacterial dry weight mass ratio of 1:5-5:1, an illumination intensity of 4000-6000lx, and a hydraulic detention time of 2-3 days.    USE - Method for denitrogenation and phosphorus-removal of town sewage.    ADVANTAGE - The method enables realizing denitrogenation and phosphorus-removal of town sewage in a simple and efficient manner with better town sewage treatment effect, achieving the indexes of ammonia nitrogen, total nitrogen, total phosphorus, chemical oxygen demand and suspended solids in the treated town sewage to the first grade A standard of the municipal wastewater treatment plant pollutant discharge standard (GB18918-2002).
NOVELTY - A liquid fertilizer contains 75-85 pts. wt. fresh sisal hemp wastewater, 15-20 pts. wt. inorganic fertilizer, 5-10 pts. wt. composite amino acid, 0.5-1 pt. wt. trace elements, 0.1-0.5 pt. wt. water retention agent and 0.05-0.1 pt. wt. plant insect repellent. The inorganic fertilizer comprises nitrogen, phosphorus and potassium in mass ratio of 15-20:5-10:5-10. The sisal wastewater is obtained by squeezing out Agave sisal wastewater, filtering wastewater and extruding sisal wastewater the same day.    USE - Liquid fertilizer is used for cultivating broadleaves holly leaves.    ADVANTAGE - The liquid fertilizer is economically and environmentally-friendly prepared. The liquid fertilizer quickly supplies nutrients to broadleaves holly leaves, and promotes rapid growth of broadleaves holly leaves. The yield of broadleaves holly leaves is increased, using the liquid fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of liquid fertilizer.
NOVELTY - Microalgae culture apparatus comprises a microalgae reactor having an inlet and outlet for gas or liquid, removable plug, and frame, where the reactor is coated with a hydrophobic resin comprising a light-transmitting material and the plug is connected to the upper portion of the reactor.    USE - The apparatus is useful for culturing microalgae chosen from Chlorella sp., Chlorococcum sp., Spirulina sp., Haematococcus sp., Neospongiococcum sp., Scenedesmus sp. and Dunaliella sp. and in water purification apparatus (all claimed).    ADVANTAGE - The apparatus is cost-effective, does not cause pollution and increases yield of microalgae.
NOVELTY - Fertilizer comprises 100-120 parts mass cattle manure, 30-50 parts mass castor cake, 12-16 parts mass mushroom residue, 60-80 parts mass rice husk powder, 20-30 parts mass algae powder, 8-10 parts mass bacteria powder, 30-40 parts mass coal gangue, 2-4 parts mass amino acids, 40-60 parts mass bentonite, 20-30 parts mass distillers grains, 40-50 parts mass crushed grass, and 80-100 parts mass water.    USE - As fertilizer for black bean (claimed).    ADVANTAGE - The fertilizer is cost-effective, and environmentally-friendly, and leaves no residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves, crushing the above-mentioned materials, stirring the crushed mixture, adding water to the mixture, fermenting the mixture for 4-6 days after sealing, allowing the mixture to stand for 12 hours, and granulating the mixture.
NOVELTY - Fertilizer comprises 60-70 parts mass sheep manure, 40-50 parts mass horse manure, 12-14 parts mass humic acid, 60-80 parts mass plant ash, 18-22 parts mass shellfish shell powder, 3-5 parts mass molasses, 0.5-0.7 part mass yeast, 30-40 parts mass bauxite, 20-30 parts mass mica powder, 50-60 parts mass Ailanthus, 30-50 parts mass Datura flower and 130-150 parts mass water.    USE - The fertilizer is useful for pomegranate flower (claimed).    ADVANTAGE - The fertilizer improves growth of the plant, and supplies nutritional components required by plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing the above-mentioned components except water, adding water to crushed components, fermenting obtained mixture for 4-6 days, maintaining fermented product at static condition for 11 hours, and granulating the product using granulator.
NOVELTY - A tea tree fertilizer comprises 80-100 pts. wt. tea cakes, 40-50 pts. wt. duck manure, 20-22 pts. wt. ammonium sulfate, 15-17 pts. wt. diammonium phosphate, 12-14 pts. wt. potassium sulfate, 15-17 pts. wt. sawdust, 8-10 pts. wt. barley straw, 20-30 pts. wt. bean stalks, 100-120 pts. wt. wheat straw, 2-4 pts. wt. composting agent and 50-60 pts. wt. water.    USE - Tea tree fertilizer (claimed).    ADVANTAGE - The tea tree fertilizer has high nutritional balance, and improves quality of tea and soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of tea tree fertilizer.
NOVELTY - A sugarcane fertilizer comprises 300-500 pts. wt. plant ash, 100-200 pts. wt. peanut cake, 600-1000 pts. wt. fermented livestock manure, 5-10 pts. wt. potassium dihydrogen phosphate, 10-20 pts. wt. potassium nitrate, 3-5 pts. wt. borax, 8-15 pts. wt. manganese sulfate and 6-10 pts. wt. zinc sulfate.    USE - Sugarcane fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sugarcane fertilizer.
NOVELTY - Producing fertilizer, by (a) mixing sheep manure, straw, tea leaves and chitosan, and fermenting, (b) obtaining monosodium glutamate waste comprising nitrogen, phosphorus and potassium content, glutamic acid, sodium salt of alanine, phenylalanine, aspartic acid and total amino acids, and (c) mixing the products obtained in steps (a) and (b), drying, mixing with urea, diammonium phosphate, potassium chloride, boron, charcoal powder, sepiolite, amino acids, microbial inoculum, and binder, stirring, drying, pulverizing, granulating, drying, and packaging product.    USE - The method is useful for producing fertilizer for preventing black spot diseases of rose plant (claimed) and controlling diseases caused by insect pests.    ADVANTAGE - The produced fertilizer reduces dosage amount of pesticide.    DETAILED DESCRIPTION - Method for producing fertilizer, involves (a) mixing 15-20 pts. wt. sheep manure, 12-15 pts. wt. straw, 5-8 pts. wt. tea leaves and 1-2 pts. wt. chitosan, and fermenting the mixture, (b) obtaining monosodium glutamate waste comprising 3-8% nitrogen, phosphorus and potassium content, 1-4% glutamic acid, 0.5-1% sodium salt of alanine, 0.1-0.2% phenylalanine, 0.1-0.5% aspartic acid and 5-10% total amino acids, and (c) mixing the products obtained in steps (a) and (b), drying until moisture content reaches less than 60%, mixing with 20-25 pts. wt. urea, 12-15 pts. wt. diammonium phosphate, 10-15 pts. wt. potassium chloride, 1-2 pts. wt. boron, 5-8 pts. wt. charcoal powder, 1-2 pts. wt. sepiolite, 3-5 pts. wt. amino acids, 1-2 pts. wt. microbial inoculum, and 0.5-1 pt. wt. binder, stirring, drying, pulverizing, granulating, drying at low temperature, and packaging obtained product.
NOVELTY - Special fertilizer is prepared using 19-21 parts mass duckweed manure, 14-16 parts mass soybean manure, 10-12 parts mass cattle manure, 7-9 parts mass potassium ore, 8-10 parts mass phosphate, 11-13 parts mass castor cake fertilizer, 4-6 parts mass lake mud, 5-7 parts mass zinc oxide, 2-4 parts mass furfural residue, 6-8 parts mass plant ash, 3-5 parts mass boric acid, 4-6 parts mass photosynthetic bacteria, and 50-70 parts mass water.    USE - As special fertilizer for water chestnut.    ADVANTAGE - The special fertilizer ensures to improve soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the special fertilizer, which involves mixing the above-mentioned raw materials for 35 minutes, allowing the mixed material to stand for 7.5 hours, and drying the mixed material to obtain product.
NOVELTY - Fertilizer comprises 22-24 pts. wt. nitrogen fertilizer, 20-22 pts. wt. phosphate fertilizer, 16-18 pts. wt. potassium fertilizer, 11-13 pts. wt. slaked lime powder, 15-17 pts. wt. horse manure, 7-9 pts. wt. kiln dust, 5-7 pts. wt. zinc chloride, 4-6 pts. wt. indole butanoate, 8-10 pts. wt. copper oxide, 2-4 pts. wt. boron residues, 3-5 pts. wt. green manure, 2-6 pts. wt. trioxide, 1-3 pts. wt. antibiotic fertilizer and 40-60 pts. wt. water.    USE - The fertilizer is useful for hawthorn (claimed).    ADVANTAGE - The fertilizer increases soil fertility and yield of hawthorn.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned raw materials for 15 minutes, and drying and granulating mixture.
NOVELTY - Ethyl acetate solvent is added to the mixture of aminophenol and sodium bicarbonate, stirred at room temperature, 3-chloropropionyl chloride is dripped in the resulting mixture to obtain 3-chloro-N-(3-hydroxyphenyl)propanamide. Aluminum chloride and N,N-dimethylacetamide are added to 3-chloro-N-(3-hydroxyphenyl)propionamide, heated, intramolecular Friedel-Crafts alkylation reaction is carried out and cyclized to obtain 7-hydroxy-3,4-dihydro-2-(1H)quinolone.    USE - Preparation of 7-hydroxy-3,4-dihydro-2-(1H)quinolone (claimed).    ADVANTAGE - The method provides 7-hydroxy-3,4-dihydro-2-(1H)quinolone with high yield, by simple, economical and environmentally-friendly process.
NOVELTY - A polyglutamic acid-phosphate compound (I), is new.    USE - New polyglutamic acid-phosphate compound is used in fertilizer.    ADVANTAGE - The new polyglutamic acid-phosphate compound can be prepared by environmentally-friendly process. The fertilizer containing new polyglutamic acid-phosphate compound has excellent usability, and promotes growth of crops.    DETAILED DESCRIPTION - A polyglutamic acid-phosphate compound of formula (I), is new.    m=1-9;    n=20-100;    R1=metal ion or phosphate/its derivative;and    R2=phosphate or its derivative.    An INDEPENDENT CLAIM is included for preparation of polyglutamic acid-phosphate compound (I).
NOVELTY - Fertilizer comprises 20-30 pts. wt. nitrogen, phosphorus, and potassium inorganic fertilizer, 20-30 pts. wt. ammonium humate, 5-10 pts. wt. biogas slurry, 30-55 pts. wt. biogas residue, 0.3-2 pts. wt. microbial inoculum and 5-15 pts. wt. bentonite.    USE - As fertilizer.    ADVANTAGE - The fertilizer improves soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves mixing the above-mentioned raw materials, adding hot water of 60-75 degrees C to the mixture, maintaining mixture for 36-60 hours, granulating mixture, drying granule, naturally cooling granule, and packaging product.
NOVELTY - Soilless cultivation substrate comprises 280-380 pts. wt. bagasse, 240-360 pts. wt. peanut shells, 300-400 pts. wt. straw, 200-300 pts. wt. dried cow dung, 120-180 pts. wt. peat, 20-35 pts. wt. urea, 22-38 pts. wt. potassium sulfate, 5-10 pts. wt. magnesium sulfate, 4-8 pts. wt. sodium nitrate, 2-5 pts. wt. copper sulfate, 4-10 pts. wt. calcium carbonate, 30-35 pts. wt. ammonium dihydrogen phosphate, 2-4 pts. wt. ammonium molybdate and 1-3 pts. wt. zinc sulfate.    USE - The soilless cultivation substrate for tomatoes (claimed) is useful for controlling diseases caused by insect pests.    ADVANTAGE - The soilless cultivation substrate is rich in nutrients, and increases yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the substrate, which involves crushing bagasse, peanut shells, and straw, adding the dried cow dung and peat, mixing, covering with plastic film, composting, fermenting at 55 degrees C, turning the mixture once every 5-7 days, maintaining at 55-65 degrees C, adding the remaining materials to the fermented product and mixing uniformly.
NOVELTY - A bio-organic material-coated fertilizer comprises 34-37 pts. wt. chicken manure, 23-26 pts. wt. duck manure, 12-16 pts. wt. bean cake, 13-15 pts. wt. peat, 18-25 pts. wt. calcium superphosphate, 10-15 pts. wt. polybutylene succinate, 12-17 pts. wt. bran powder, 10-14 pts. wt. straw powder, 14-16 pts. wt. corn meal, 21-24 pts. wt. mung bean stalk powder, Sorghum meal, ammonium chloride, potassium chloride, potassium humate, magnesium sulfate, chitin, hydroxymethyl starch, cellulolytic bacteria, effective microorganism microbial inoculant, soil conditioner and water.    USE - Bio-organic material-coated fertilizer is used for strawberry.    ADVANTAGE - The bio-organic material-coated fertilizer improves soil fertility, soil compaction and quality of strawberry.    DETAILED DESCRIPTION - A bio-organic material-coated fertilizer comprises 34-37 pts. wt. chicken manure, 23-26 pts. wt. duck manure, 12-16 pts. wt. bean cake, 13-15 pts. wt. peat, 18-25 pts. wt. calcium superphosphate, 10-15 pts. wt. polybutylene succinate, 12-17 pts. wt. bran powder, 10-14 pts. wt. straw powder, 14-16 pts. wt. corn meal, 21-24 pts. wt. mung bean stalk powder, 9-13 pts. wt. Sorghum meal, 23-27 pts. wt. ammonium chloride, 13-15 pts. wt. potassium chloride, 13-15 pts. wt. potassium humate, 1-3 pts. wt. magnesium sulfate, 0.3-0.7 pts. wt. chitin, 2-4 pts. wt. hydroxymethyl starch, 0.3-0.8 pts. wt. cellulolytic bacteria, 6-10 pts. wt. effective microorganism microbial inoculant, 8-13 pts. wt. soil conditioner and remainder of water. An INDEPENDENT CLAIM is included for manufacture of bio-organic material-coated fertilizer.
NOVELTY - An organic and inorganic fertilizer comprises 180-220 pts. wt. sugar residue, 18-25 pts. wt. mineral element as amino acid chelate, 25-35 pts. wt. fulvic acid, 45-60 pts. wt. binder, 220-250 pts. wt. urea, 170-200 pts. wt. monoammonium, 80-90 pts. wt. potassium chloride, 180-210 pts. wt. ammonium sulfate, 20-50 pts. wt. insecticidal bacteriostat agent, 0.5-0.6 pt. wt. dispersant, 0.5-1 pt. wt. disintegrant, 0.5-0.6 pt. wt. synergist and 0.6-1 pt. wt. penetrant.    USE - Organic and inorganic fertilizer (claimed).    ADVANTAGE - The environmentally-friendly organic and inorganic fertilizer has excellent plant resistance, pest resistance and disease resistance, and is rich in nutrients.    DETAILED DESCRIPTION - An organic and inorganic fertilizer comprises 180-220 pts. wt. sugar residue, 18-25 pts. wt. mineral element as amino acid chelate, 25-35 pts. wt. fulvic acid, 45-60 pts. wt. binder, 220-250 pts. wt. urea, 170-200 pts. wt. monoammonium, 80-90 pts. wt. potassium chloride, 180-210 pts. wt. ammonium sulfate, 20-50 pts. wt. insecticidal bacteriostat agent, 0.5-0.6 pt. wt. dispersant, 0.5-1 pt. wt. disintegrant, 0.5-0.6 pt. wt. synergist and 0.6-1 pt. wt. penetrant. The insecticidal bacteriostat agent contains 3-5 pts. wt. pyrethrum, 8-10 pts. wt. mint leaves, 4-6 pts. wt. pepper leaves, 3-5 pts. wt. clove, 3-5 pts. wt. neem and 9-12 pts. wt. phytosterol. An INDEPENDENT CLAIM is included for preparation of organic and inorganic fertilizer.
NOVELTY - Bio-fertilizer comprises 10-60 pts. wt. charcoal powder, 20-80 pts. wt. compost, 2-10 pts. wt. humic acid, 2-10 pts. wt. amino acid component, 0.2-2 pts. wt. biological agent, and 0.2-0.5 pts. wt. carrier.    USE - The bio-fertilizer is useful for repairing heavy metal contaminated soil.    ADVANTAGE - The bio-fertilizer enables to increase yield and quality of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves weighing the above-mentioned raw materials, and mixing weighed raw materials uniformly to obtain the product.
NOVELTY - Hydrocortisone as feedstock is added to dimethylformamide as solvent. P-toluenesulfonic acid is added to mixture and catalyzed, to obtain cyclic triethyl ester. Cyclic triethyl ester is dissolved in methanol-water mixed solvent, hydrolyzed in dry-hydrogen catalytic solid acid resin or silica-supported acid catalyst, to obtain hydrocortisone butyrate.    USE - Preparation of hydrocortisone butyrate (claimed).    ADVANTAGE - The method enables economically and environmentally-friendly preparation of hydrocortisone butyrate with high selectivity and yield under mild reaction conditions, with reduced equipment requirements and generation quantity of industrial acid wastewater and byproducts, and without adhesion of catalyst.
NOVELTY - The method involves mixing high-sulfur coal having a particle size of 5 mm, water vapor as gasification agent and oxidizing agent, subjecting the mixture to gasification at 1100-1300 degrees C, preferably 1150-1250 degrees C and a pressure of 3-4 MPa, preferably 3.4-3.8 MPa to obtain crude methanol, and purifying crude methanol by washing.    USE - The method is useful for preparing methanol from high-sulfur coal (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of high-sulfur coal for preparing methanol.
NOVELTY - A imidazole-based ionic salt (I), is new.    USE - New imidazole-based ionic salt (claimed).    ADVANTAGE - The imidazole-based ionic salt is manufactured by simple and environmentally-friendly process.    DETAILED DESCRIPTION - A imidazole-based ionic salt of formula (I), is new.    R=NH3, HNO3 or group of formula (i).    An INDEPENDENT CLAIM is included for preparation of imidazole-based ionic salt (I).
NOVELTY - Method for preventing and controlling weeds in paddy field, involves transplanting the rice seedlings to field, mixing aqueous dispersion of metolachlor and oxadiazon powder, adding water to the mixture, spraying after 7 days, and maintaining water level to 3-5 cm from surface for 4-6 days.    USE - The method is used for preventing and controlling weeds in paddy field (claimed).    ADVANTAGE - The method is environmentally-friendly and cost-effective.
NOVELTY - Traditional Chinese medicine comprises 10-15 pts. wt. Asprella, 0.2-0.5 pt. wt. terramycin powder, 5-8 pts. wt. Gynostemma herb, 10-15 pts. wt. balloon flower, 5-8 pts. wt. rhizoma coptidis, 0.1-0.3 pt. wt. arts pefloxacin mesylate soluble powder, 6-9 pts. wt. selenium-enriched yam, and 6-10 pts. wt. Ageratum.    USE - The traditional Chinese medicine is useful for clearing heat, removing toxins, preventing flu, viral hepatitis and cholera, increasing immunity, and preventing and/or treating plague, dysentery and cold in goose.    ADVANTAGE - The traditional Chinese medicine is prepared environmentally-friendly, and improves taste and smell of the goose meat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned traditional Chinese medicine, which involves selecting the above-mentioned raw materials, washing ad drying the above-mentioned materials at 50-60 degrees C, crushing the mixture to mesh size of 100, blending the mixture excluding terramycin powder and pefloxacin mesylate soluble powder, adding the terramycin powder and pefloxacin mesylate soluble powder to the obtained mixture, and packing, bottling and sealing the obtained mixture.
NOVELTY - Feed comprises main material and additive, where the main material comprises corn, soybean, soybean meal, fish meal, Perilla oil, whey powder, calcium hydrogen phosphate, calcium carbonate, and edible salt, and the additive component contains trace mineral premix, pig milk with multivitamins, enzyme complex, pepsin, probiotic composition, vitamin E, vitamin C, butyric acid, amino acid, methionine, threonine, arginine, sucrose and mannitol oligosaccharide, Sophora flavescens powder, radix sophorae flavescentis, and sweet wormwood powder.    USE - The feed is useful for preventing diarrhea and dysentery in piglet (claimed).    DETAILED DESCRIPTION - Feed comprises main material and additive, where the main material comprises 52.5-62 wt.% corn, 7-12 wt.% soybean, 13-20 wt.% soybean meal, 4-5.5 wt.% fish meal, 1-2 wt.% Perilla oil, 3-5 wt.% whey powder, 1.5-2.5 wt.% calcium hydrogen phosphate, 0.2-1 wt.% calcium carbonate, and 0.3-0.4 wt.% edible salt, and the additive component (1 ton) comprises 2000-3000 g trace mineral premix, 150-250 g pig milk with multivitamins, 2000-2500 g enzyme complex, 100-200 g pepsin, 1500-2500 g probiotic composition, 100-200 g vitamin E, 150-300 g vitamin C, 2000-3000 g butyric acid, 100-2500 g amino acid, 600-1000 g methionine, 600-800 g threonine, 1200-1500 g arginine, 2000-3000 g sucrose and mannitol oligosaccharide, 2000-3500 g Sophora flavescens powder, 2000-3500 g radix sophorae flavescentis, 1500-2500 g Astragalus powder, and 10000-15000 g sweet wormwood powder. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned feed, which involves mixing the above-mentioned raw materials, uniformly stirring the mixture, and spraying the stirred mixture.
NOVELTY - Synthesis of aromatic alkyne comprises reacting sulfuryl fluoride and 2-trialkyl or aryl silicon-based phenol in methylene chloride solvent in the presence of triethylamine catalyst at room temperature for 0.5-8 hours, removing solvent, and separating and purifying through silica gel column chromatography to obtain aryl alkyne precursor; and reacting with alkali in organic solvent in the presence of phase transfer catalyst at - 20-80 degrees C for 8-24 hours.    USE - Method for synthesis of aromatic alkyne (claimed).    ADVANTAGE - The method is simple, achieves high yield, and it has low substrate fluorine atom content, reduced cost and environmental pollution, easy to obtain raw materials, and mild reaction condition.
NOVELTY - Method for constructing urban landscape water ecosystem, involves removing sludge, sterilizing, activating, controlling water level to depth of not greater than 0.5 m, aerating for 1-2 days, adjusting pH to 8 or less, dividing into deep water area and region around the deep water area, planting seasonal plants and submerged plants in the deep water area, controlling water level to 0.7-1.2 m, dropping 2-8 algae-eating insects, raising the water level until it reaches normal level, maintaining for 15-45 days and feeding aquatic animals.    USE - The method is used for constructing urban landscape water ecosystem (claimed).    ADVANTAGE - The method improves quality and transparency of water, and eliminates growth of blue-green algae.    DETAILED DESCRIPTION - Method for constructing urban landscape water ecosystem, involves removing sludge, sterilizing, activating, controlling water level to depth of not greater than 0.5 m, aerating for 1-2 days, adjusting pH to 8 or less, dividing into deep water area and region around the deep water area, where 10-40% of area is deep water area and 60-90% of area is region around the deep water area, planting seasonal plants and submerged plants in the deep water area, controlling water level to 0.7-1.2 m, dropping 2-8 algae-eating insects, raising the water level until it reaches normal level, maintaining for 15-45 days and feeding aquatic animals.
NOVELTY - Culturing Hericium erinaceus, involves (a) preparing substrate by mixing biogas residue, rapeseed cake, chicken manure, gypsum and phosphate fertilizer, (b) staking obtained mixture, (c) allowing fermentation of stacked material, (d) forming cultivation bed using fermented product, and controlling temperature of the bed until the cultivation bed becomes less moist, (e) culturing H.erinaceus in the cultivation bed, and (f) harvesting matured H.erinaceus.    USE - The method is useful for culturing H.erinaceus (claimed).    ADVANTAGE - The method is environmentally-friendly, and utilizes waste.    DETAILED DESCRIPTION - Method for culturing Hericium erinaceus, involves (a) preparing substrate by mixing 82-88 parts biogas residues, 10-15 parts rapeseed cake, 6-8 parts chicken manure, 1.5-2.5 parts gypsum and 3 parts phosphate fertilizer, (b) staking obtained mixture to obtain heap having width of 5 m and height of 0.8-1.2 m, and covering the heap using sheet, after splashing water, (c) allowing fermentation of stacked material, measuring temperature after 7 days, where the temperature is 75 degrees C, turning the material evenly, continuing stacking for 5-6 days, controlling temperature to 80 degrees C, turning the material, and continuing stacking for 3-4 days, (d) forming cultivation bed using fermented product, where thickness of the cultivation bed is 32-38 cm, and controlling temperature of the bed at 60-65 degrees C for 72 hours until the cultivation bed becomes less moist, (e) culturing H.erinaceus in the cultivation bed at 21 degrees C, and (f) harvesting matured H.erinaceus.
NOVELTY - Preparing sodium dihydrogenphosphate fertilizer involves mixing urea and phosphoric acid in molar ratio of 2.3:2.5-3 and then heating at 136-141 degrees C for 2.6 hours to form a mixture. Sodium hydroxide is added into the mixture to adjust the pH to 3.7-3.9. The mixture comprises 15.1-15.4 % nitrogen, 7.1-7.4 % phosphorus pentoxide and 4.1-4.4 % sodium. The mixture is cooled to obtain crystal and filtered to obtain filter cake. Other elements are added to the filter cake and then heated to obtain another mixture. The obtained mixture is dried at 30 degrees C for 30 minutes to obtain the product.    USE - Method for preparing fertilizer used for ramie (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a cost-effective manner and eco-friendly manner.
NOVELTY - Fertilizer composition comprises 25-27 pts. wt. rotten duck manure, 20-23 pts. wt. ammonium bicarbonate, 17-19 pts. wt. potassium chloride, 15-18 pts. wt. Bacillus preparation, 13-16 pts. wt. calcium carbonate, 11-13 pts. wt. sodium nitrophenolate, 12-16 pts. wt. potassium sulfate, 9-12 pts. wt. fat film powder, 8-10 pts. wt. zinc ammonium phosphate, 6-9 pts. wt. manganese slag, 5-9 pts. wt. copper sulfate, 3-5 pts. wt. Borax (RTM: Sodium tetraborate), 1-5 pts. wt. plant ash, 1-3 pts. wt. rice green and 50-60 pts. wt. water.    USE - Fertilizer composition used for cultivating cotton (claimed), and used for preventing and treating insect pests.    ADVANTAGE - The fertilizer composition is prepared in a simple and cost-effective manner, and ensures improved yield and quality of cotton.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves: mixing raw materials uniformly for 50 minutes to obtain the finished product.
NOVELTY - A fuel reformer (1) contains evaporation chamber (11) which generates water vapor and is filled with heat-transfer acceleration material, mixing chamber (12) which mixes fuel gas and water vapor, is connected with evaporation chamber, is filled with modification catalyst (21) and consists of space part with which heat-transfer acceleration material and modification catalyst are not filled, modification chamber (13) which modifies mixed gas from mixing chamber and generates reformed gas containing hydrogen, and communication part which is provided in a part of partition wall.    USE - A fuel reformer for fuel cell system (claimed).    ADVANTAGE - Mixing property of fuel gas and water vapor is improved, and caulking of modification catalyst in modification chamber can be suppressed.    DETAILED DESCRIPTION - A fuel reformer (1) comprises evaporation chamber (11) which generates water vapor and is filled with heat-transfer acceleration material, mixing chamber (12) which mixes fuel gas and water vapor, is connected with evaporation chamber, is filled with modification catalyst (21) and consists of space part with which heat-transfer acceleration material and modification catalyst are not filled, modification chamber (13) which modifies mixed gas from mixing chamber and generates reformed gas containing hydrogen, communication part which is provided in a part of partition wall which partitions off evaporation chamber and mixing chamber, and nozzle which produces jet stream of fuel gas and water vapor to mixing chamber interior. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel reformer. (Drawing includes non-English language text).    Fuel reformer (1)    Evaporation chamber (11)    Mixing chamber (12)    Modification chamber (13)    Modification catalyst (21)
NOVELTY - Recycling agricultural crop residues involves cutting straw to a length of 3-15 cm, and then performing steam explosion for straw pre-treatment. Solid state fermentation is performed, where ammonia, peptone, wheat bran, straw of certain size, peanut, adjust and aerobic digesters are introduced into the fermenter. The solid state fermentation is performed at 20-55 degrees C for 10-20 days to produce to obtain waste activated sludge, which then squeezed to remove water from it. The squeezed to obtain waste activated sludge is dried at certain temperature to obtain dehydrated fermentation residues.    USE - Method for recycling agricultural crop residues (claimed).    DETAILED DESCRIPTION - Recycling agricultural crop residues involves cutting straw to a length of 3-15 cm, and then performing steam explosion for straw pre-treatment. Solid state fermentation is performed, where ammonia, peptone, wheat bran, straw of certain size, peanut, adjust and aerobic digesters are introduced into the fermenter. The solid state fermentation is performed at 20-55 degrees C for 10-20 days to produce to obtain waste activated sludge, which then squeezed to remove water from it. The squeezed to obtain waste activated sludge is dried at certain temperature to obtain dehydrated fermentation residues. The dehydrated fermentation residues are pulverized to obtain activated carbon, where the unfermented product is treated with phosphoric acid or potassium chloride. The agricultural crop residues are selected from wheat bran, rice, corn, soybeans and other crop stalks.
NOVELTY - The electrolyzer (10) has an anode electric power feeding housing (40) that is provided as an electrolysis portion (44) provided with opening portion (44h) to circulate water to anode catalyst layer (40a). A frame (46) is arranged in the outer periphery of the electrolysis portion more precisely than electrolysis portion. The anode catalyst layer is provided only in the range of the electrolysis portion. A cathode catalyst layer (42a) is formed with the range to oppose the anode catalyst layer and to oppose the frame.    USE - Differential pressure type high-pressure water electrolyzer.    ADVANTAGE - The cathode catalyst layer is provided over the range which opposes a frame while having a bigger area than an anode catalyst layer, when water moves to a cathode side in connection with a proton moving from an anode side at the time of electrolysis. Thus, the solid polymer electrolyte membrane ensures a desired film water retention value, and it becomes possible to effectively prevent the film damage by electrolysis. Hence, the drying of solid polymer electrolyte membrane is suppressed as much as possible, and the deterioration of solid polymer electrolyte membrane can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the differential pressure type high-pressure water electrolyzer.    Differential pressure type high-pressure water electrolyzer (10)    Anode electric power feeding housing (40)    Anode catalyst layer (40a)    Cathode catalyst layer (42a)    Opening portion (44h)    Frame (46)
NOVELTY - Processing of lignocellulosic biomass involves providing lignocellulosic biomass and solvent(s), providing and heating a mixer to a temperature of 100-300 degrees C, adding biomass and solvent to the mixer, mixing biomass and solvent into a biomass slurry, and melt-compounding the biomass slurry under shearing and heating for an amount of time to cause disruption of inter- or intra-polymer linkages of the biomass.    USE - Processing of lignocellulosic biomass used for producing fermentable sugar e.g. oligosaccharides and monosaccharides.    ADVANTAGE - The lignin is efficiently extracted and converted into useful sugars at high conversion rates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition, which comprises lignin having a number average molecular weight (Mn) of 1000-10000 daltons, and a phenolic hydroxyl content.
NOVELTY - The equipment has hydrogen gas bucket (1) that is connected with first tubular element (11) and whose inner portion is stored with hydrogen gas. A solution bucket (2) is connected with second tubular element (21) and whose inner portion is stored with solution. The atomization units (3) are connected with the solution bucket by second tubular element, and are provided for atomizing the fluid ejected with the form of small molecule. A temporary storage bucket (4) is connected at the exit of atomization units and is connected with first tubular element.    USE - Hydrogen solution manufacturing equipment.    ADVANTAGE - The hydrogen gas and the solution can be mixed fully for manufacturing hydrogen solution. The manufacturing process of the hydrogen solution can be simplified and the cost can be reduced. The pressure of the hydrogen gas can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen solution manufacturing equipment.    Hydrogen gas bucket (1)    Solution bucket (2)    Atomization units (3)    Temporary storage bucket (4)    Tubular elements (11,21)
NOVELTY - Preparing organic fermented fertilizer involves utilizing mixture of organic waste, moisture-content adjustment material and effective microorganism materials, and then ground bamboo is added to obtain paste. Anaerobic fermentation of the paste is carried out and then ground by a high-speed grinder. The fermentated product is dried, pelletized and molded.    USE - Method for preparing organic fermented fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fermented fertilizer in a short period of time, and has wide industrial applicability.
NOVELTY - The electrolyzer (10) has an anode electric power feeding portion (42) that is provided with a support sheet portion (48) which supports a protection sheet portion (46). A through-hole (52a) which is provided with bigger opening area than a through-hole (46a) of the protection sheet portion is formed in the support sheet portion. A through-hole (54) which is provided with bigger opening area than a through-hole (52b) of the support sheet portion is formed in a water current sheet portion (50) which carries out the current of the water for electrolysis.    USE - Differential pressure type high-pressure water electrolyzer for generating hydrogen gas for use as fuel gas for electric-power-generating fuel cell.    ADVANTAGE - The anode electric power feeding portion is stacked with the support sheet portion which supports a protection sheet portion, and the water current sheet portion that maintains the current of the water for electrolysis. Hence favorable water flow distribution property and voltage resistance are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the differential pressure type high-pressure water electrolyzer.    Differential pressure type high-pressure water electrolyzer (10)    Anode electric power feeding portion (42)    Protection sheet portion (46)    Through-holes (46a,52a,52b,54)    Support sheet portion (48)    Water current sheet portion (50)
NOVELTY - The liquefier has a liquefier body (1) provided with a filter for filtering dust and solid impurities. A compressor (2) and a sieve purifier (3) are connected with each other. The sieve purifier removes water vapor and carbon dioxide of biogas, where biogas enters a rectifying tower. Different boiling point fractionation processes are performed by biogas, where boiling point of liquid methane is greater than that of liquid nitrogen.    USE - Green energy pneumatic biogas liquefier.    ADVANTAGE - The liquefier utilizes rich coal to develop alternative energy sources so as to save energy and reduce emission rate in an environment-friendly manner, and reduces processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a green energy pneumatic biogas liquefier. '(Drawing includes non-English language text)'    Liquefier body (1)    Compressor (2)    Sieve purifier (3)    Cooling tower (5)    Liquid tank (7)
NOVELTY - This new utility model claims of one monitoring biological treatment of waste water of experiment device, comprising water tank, inside the water tank bottom equipped with aeration device, the aeration device and air pump through pipeline communicated outside, the water tank upper part set with water for mouth, bottom set with water outlet port, the water tank top provided with dissolve oxygen online detection device, the air pump via voltage-stabilizing power supply and trigger and the dissolve oxygen online detection device electric connection, after the air pump of pipeline is equipped with air flow meter and CO2 detection device, of the water tank also equipped with COD sampling port and CO2 or methane detecting port, this new utility model claims that the device can simulate different and sewage treatment method, saves cost, is easy to manage.
NOVELTY - This utility new type relates to sewage treatment device field, especially relates to one used for salt alkali o a salt alkali water treatment of Ecological landscape floating island wetland, comprising separating pool, an isolation pool centre form the water planting of floating plant area, water area periphery forming a secondary water, the secondary water purifying area periphery forming a primary purifying, convex edge are cloth has connected salt alkali water inlet of the primary water, for purifying a provided with connected water outlet at the bottom of the water area, inner primary net water area provided with fill zeolite is zeolite basket, a secondary net water area by the bottom in turn provided with inner layer stone, stone and sand layer and earthworm cultivation, planting the planting earth layer, the planting layer and primary purifying the bottom level is b., inner stone layer has through aeration pipe along the planting soil layer above a wound setting a spraying pipe, inner water area set with spray pipe of a water pump water. This utility new type having low cost, a thermostability alkali water purification effect is good, a salt alkali water for taking fully use, which increases the green area soil is equal.
NOVELTY - This utility new type provide a one used for sewage and wastewater treatment of microorganism treatment device, comprising a, water storage tank, for storage sewage or waste water, a room, used for sewage or waste water for removing nitrogen treatment process and filter the activated strain, culture room, select corresponding culture medium, culture activity in strain in this medium, a microorganism strengthening nutrient liquid, and this microorganism for strengthening nutrition liquid discharging purification pool, purification pool, for sewage and waste water in a water storage pool using a microorganism strengthening nutrition liquid carry out purification treatment, a precipitation room, a water outlet in purification pool for mud-water separating treatment process, a sludge return to tank, entering into water pool, water tank, used for biochemical water for carrying out CL inorganic flocculating detection, according to detection result adjustment in culture room microorganism strengthening concentration or variety of nutrient liquid. This utility new type through specific microorganism for carrying out strengthened culture, more economical and more efficient increase the water quality of sewage water processing system.
NOVELTY - Propylene glycol based fuel in an open geometry wicked device, comprises at least 60 wt.% propylene glycol. The propylene glycol based fuel has a flashpoint above 50 degrees C.    USE - The propylene glycol based fuel is useful as a safe fuel; for lighting a barbecue; and in decorative home furnaces containing a chimney (all claimed).    ADVANTAGE - The propylene glycol based fuel is much safer in use than other used fuels. It does not produce toxic emissions, or at least hardly produces such emissions. The sketched safety risks associated with ventless ovens are resolved by using a much safer fuel that does not explode during refueling a burning system, yet is combustible. For example, when refilling a burning fire place, no explosion of flash flame will occur. Also, when, for example, a ventless fireplace falls over and spills the fluid over the floor, the fire will generally extinguish by itself or will be easy to extinguish.
NOVELTY - The bioreactor has a single-chamber steel container formed with a man-hole and mounting studs for connecting external devices. An outer part of a drum part (1) is driven by a motor (10) for a drum pendulum motion when the drum part is controlled by a sensor (11). The drum part is provided with a heating pipe system (9) and a pipe (7) at an inner portion for supplying stabilizing agent to an injector (8).    USE - Bioreactor for disposal of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bioreactor.    Drum part (1)    Pipe (7)    Injector (8)    Heating pipe system (9)    Motor (10)    Sensor (11)
NOVELTY - The reactor (1) has a grid that is arranged in reactor interior, in rust housing (5), such that metered gasified fuel is formed as fixed bed. A raised rust cone is located centrally in grid as rust pyramid having pyramid corners formed with adjacent pyramid faces. A carrier paddle is arranged in side wall portion.    USE - Fixed bed reactor for gasification of fuel such as biomass and waste material e.g. wood.    ADVANTAGE - The production engineering and production technology of reactor are improved. The material flow in the reactor interior is significantly more uniform. The efficiency of the reaction effect is improved. The material-saving property is realized in simple manner. The design flexibility is improved.    DESCRIPTION OF DRAWING(S) - The drawings show the top perspective view and side view of the fixed bed reactor.    Reactor (1)    Rust housing (5)    Reactor lining (7)    Muffle tube (12)    Reactor housing (22)
NOVELTY - The reactor (1) has an inside wall that is provided from spaced air inlet openings. The air or water vapor or oxygen enriched air is supplied via oxidation zone gasification unit. A limiting element is arranged, while forming an annular oxidation zone. A defined gap (85) is formed at certain distance with the inner wall and is formed with the air inlet openings. A limiting element comprises one oxidation zone of the associated outlet opening in which gasifying agent is supplied via the annular oxidation zone.    USE - Fixed bed reactor for gasification of fuels such as carbonaceous solid fuels for biomass or waste materials such as timber or substances.    ADVANTAGE - The quality of the product gases received is increased and/or optimized on straightforward and operator-safe way, as the limiting element comprises one oxidation zone of the associated outlet opening in which gasifying agent is supplied via the annular oxidation zone.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic and side view of the fixed bed reactor.    Fixed bed reactor (1)    Rust housing (5)    Internal reactor wall (7)    Muffle tube (12)    Gap (85)
NOVELTY - The fixed bed reactor (1) has a lower muffle tube end area which protrudes as free muffle tube end area spaced from a reactor-inner wall in a reactor inner space. An upper reactor-inner wall area surrounds the lower, free muffle tube end area with a defined gap distance. The upper reactor-inner wall area is seen in vertical axis direction. A gas reservoir is formed between the lower, free muffle tube end area and the upper reactor-inner wall area.    USE - Fixed bed reactor for the gasification of fuels, particularly biomass.    ADVANTAGE - The fixed bed reactor has a lower muffle tube end area which protrudes as free muffle tube end area spaced from a reactor-inner wall in a reactor inner space, and thus ensures simple and efficient gasification of the fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a fixed bed reactor.    Fixed bed reactor (1)    Reactor-lining (7)    Muffle tube (12)    Reactor housing (22)    Head part (85)
NOVELTY - The fixed bed reactor (1) comprises a reactor inner space which is mounted with a rotatable rust plate, and a raised rust cone which is mounted at the center of the rust plate. The apex of the rust cone is provided with a tower-like agitator, in which a muffle tube (12) protrudes upwards of the conical tip, especially towards the interior of the reactor, along the vertical axis direction.    USE - Fixed bed reactor for gasification of fuels such as biomass and other waste materials such as wood, etc.    ADVANTAGE - The reactor has a simple structure, and mixing of bulk materials is carried out in a simple and reliable manner.    DESCRIPTION OF DRAWING(S) - The drawings show a schematic perspective external view of a fixed bed reactor, and a schematic side view of the fixed bed reactor.    Fixed bed reactor (1)    Rust housing (5)    Reactor lining (7)    Muffle tube (12)    Head portion (85)
NOVELTY - The surplus sludge fermentation coupled biological nitrogen removal device has a fermenting sludge discharging pump (4-5) that is connected with a fermentation liquid separating chamber (5).The fermentation liquid separating chamber is provided with a fermentation liquid separating sludge chamber (5-1), and a fermentation liquid pump (5-2). A struvite recovery chamber (6) is connected with a nitrogen and phosphorus removal chamber. The struvite recovery chamber is connected with a raw water tank (7) through a carbon source pump (6-4).    USE - Surplus sludge fermentation coupled biological nitrogen removal device.    ADVANTAGE - The sludge discharge amount of the biological nitrogen removal device is reduced. The reliability of the biological nitrogen removal device is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a surplus sludge fermentation coupled biological nitrogen removal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the surplus sludge fermentation coupled biological nitrogen removal device.    Fermenting sludge discharging pump (4-5)    Fermentation liquid separating chamber (5)    Fermentation liquid separating sludge chamber (5-1)    Fermentation liquid pump (5-2)    Struvite recovery chamber (6)    Carbon source pump (6-4)    Raw water tank (7)
NOVELTY - Pre-processing lignocellulose comprises: (i) removing the impurities of lignocellulosic raw material, then drying, crushing and sieving; and (ii) adding the lignocellulosic material into sodium hydroxide solution (0.1-0.15 g/g of raw material), stirring uniformly, then sequentially adding hydrogen peroxide (0.025-0.125 g/g of raw material) and cyanamide activator (0.01-0.03 g/g of raw material), then stirring uniformly to obtain mixed reaction solution, reacting the mixed reaction solution at 25-35 degrees C by stirring for 20-30 hours.    USE - The pre-processed lignocellulose is useful in preparing xylose and glucose (claimed).    ADVANTAGE - The pre-processing method improves the conversion rate of lignocellulosic sugar (claimed), is simple and does not produce intractable wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing xylose and glucose using lignocellulose, comprising: (a) regulating the pH of pre-processed lignocellulose to 4.5-5.5 using sulfuric acid, then adding antibiotics and mixing uniformly to obtain reaction solution; and (b) adding complex enzyme (57-69 wt.% cellulase, 21-33 wt.% hemicellulase and 4-16 wt.% pectinase) into the reaction solution (5.25-10.5 mg/g of lignocellulose) and reacting at 45-50 degrees C by stirring for 20-30 hours, centrifuging and collecting the supernatant containing xylose and glucose solution.
NOVELTY - The system has a separator system (84) that is provided in communication with a hopper for receiving organic waste from hopper. A wash water liquid tank is communicated with separator system. A product tank is communicated with separator system for receiving organic waste from separator system. A make-up product tank is communicated with separator system for receiving organic waste from separator system having low COD. A portion of the organic waste from the make-up product tank is periodically injected into the product tank upon request.    USE - Organic waste processing system for producing slurry used for production of bio-gas, transportation fuels or chemical products, and residual solid.    ADVANTAGE - The cost associated with the processing, transport and ultimate disposal of the organic waste materials is reduced. The organic waste processing system produces consistent, high quality feedstock that can be safely added to an anaerobic digestion process, or fuel/chemical process and which can increase methane gas production, transportation fuels, other beneficial chemicals, and maximizes diversion of organic waste from landfills. The multi-tank system produces a consistent fuel product and reduces the amount of landfilled waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing organic waste slurry for production of bio-gas, transportation fuels or chemical products.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of organic waste processing system.    Separator system (84)
NOVELTY - Producing hydrogen by dark fermentation from organic material, comprises introducing organic material and microorganisms into completely mixed bioreactor for breaking down organic material into products including hydrogen gas, carbon dioxide gas, volatile fatty acids and alcohols by dark fermentation; continuously sequestering carbon dioxide gas within a headspace of the bioreactor for capturing the carbon dioxide as bicarbonate within the headspace; and recovering a portion of hydrogen gas from head-space under vacuum.    USE - The method and system are useful for producing hydrogen, methane, volatile fatty acids, and alcohols from organic material by dark fermentation (all claimed).    ADVANTAGE - The recovered hydrogen gas is substantially free of carbon dioxide. The system and method provide higher hydrogen production rate. The method provides reliable carbon dioxide removal from bio-hydrogen, and provides improved hydrogen yields.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is also included for a system comprising a completely mixed bioreactor for dark fermentation, an input for supplying microorganisms and the organic material to be broken down into products including hydrogen gas, carbon dioxide gas, volatile fatty acids (VFA) and alcohols, to the bioreactor, a carbon dioxide trap in a headspace of the reactor, where the trap includes a solid hydroxide for sequestration of the carbon dioxide gas from the headspace and capture of the carbon dioxide as bicarbonate within the headspace; a gas output for removal of a gas effluent including hydrogen gas from the headspace; and a liquid output for removing a first liquid effluent including at least a portion of the microorganisms, the volatile fatty acids, and the alcohols from the bioreactor.
NOVELTY - This utility new type relates to one of a retting fertilizer device, solves the problem that the organic fertilizer production in current technology a long, and it is easy to cause environment pollute problem of. device comprising a liquid fertilizer fermenting device and solid fertilizer supply device, the solid fertilizer supply device b is set above a liquid fertilizer fermenting device, set with fertilizer outlet at the bottom of a solid fertilizer supply device, a fertilizer outlet by upper end surface of baffle and liquid fermenting device of liquid fertilizer device connected, stirrer set at the bottom of liquid fermenting device of liquid fertilizer device, a stirrer provided with a thermometer, a stirrer by a control, by a combination of the control plate.
NOVELTY - The apparatus has reaction tube (33a) that receives microparticles generated by a small particle generation tube (30). Water is supplied in the reaction tube. Reacting agent (12) is accommodated in small particle generation tube. The small particle generation tube and the reaction tube are heated. The reacting agent is sodium hydroxide or potassium hydroxide. A metallic element is supplied to the reacting agent from metallic element supply structure.    USE - Hydrogen-producing apparatus used in boat and ship, for electric generating facility, hydrogen station and hydrogen fueled engine, used for producing hydrogen from water.    ADVANTAGE - The alkali-fusion salt melt first and second metal ions is accommodated in reaction container, and the small particle group is dispersed. Since small particle group has big hygroscopicity, the water vapor adsorbs the alkali metal ion such as sodium ion and potassium ion to the surface, if water vapor is made to collide with the small particle group. Hydrogen in water vapor is separated under the presence of the first metal ion such as nickel ion, palladium ion and platinum ion, and second metal ion such as chromium ion, molybdenum ion, ferric ion and tungsten so as to emit the hydrogen gas. Reaction becomes active in an anoxic state. Since oxygen does not exist at all in the state of gas, the oxygen is safe for not exploding, even if the inside of reaction container is 300 degrees C or more. The apparatus increases the amount of hydrogen. The hydrogen is collected from water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen-producing method for generating hydrogen from water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the reaction of fine granule group and water vapor.    Reacting agent (12)    Small particle generation tube (30)    Heaters (31,37)    Reaction tube (33a)    Water receptacle (35)
NOVELTY - The method involves using foodstuff waste material as raw material. The foodstuff waste material is existed at specific temperature ranges, so as to implement carbonization process at temperature from which the emitted-heat amount of organic waste fuel obtained by carbonization process in predetermined value. The process temperature is defined based on season which recovered raw materials with preset formula relating emitted-heat amount (MJ/kg) and process temperature (T). The multiple types of cooked foodstuff and/or half-cooked foodstuff are mixed as foodstuff waste material.    USE - Manufacturing method of organic waste fuel.    ADVANTAGE - The organic waste fuel manufacturing process can be handled easily, by suppressing raise of manufacturing cost.    DETAILED DESCRIPTION - The method involves discarding (S1) the material from the convenience store or/and the supermarket as each cooked foodstuff and/or a half-cooked foodstuff. The primary heat-processed material which heated the foodstuff waste material and reduced water content is obtained. The oil component of suitable amount is mixed with primary heat-processed material, and mixture is obtained. An INDEPENDENT CLAIM is included for an organic waste fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the procedure of manufacturing the organic waste fuel. (Drawing includes non-English language text)    Step to discard cooked foodstuffs and/or half-cooked foodstuffs (S1)    Step to crush package (S2)    Step to remove crushed package (S3)    Step to throw in raw material in in carbonization apparatus (S4)    Step to maintain carbonization process (S6)
NOVELTY - Fruits and vegetables biological fertilizer comprises 0.01-0.03 pt. wt. abamectin mixture, 11-13 pts. wt. ammonium dihydrogen phosphate, 9-14 pts. wt. calcium hydrophosphate, 60-75 pts. wt. chicken manure, 0.001-0.006 pt. wt. Bdellovibrio powder, 0.01-0.02 pt. wt. bacteriophage powder, 0.01-0.1 pt. wt. marine Spirillum powder, 60-70 pts. wt. sludge, 1-8 pts. wt. phosphorite powder, and 25-30 pts. wt. oyster shell powder.    USE - Fruits and vegetables biological fertilizer.    ADVANTAGE - The fertilizer promotes maturity and good color of fruits and vegetables, reduces amount of pesticide, increases yield and sweetness of fruits, and saves cost.
NOVELTY - Waste mushroom organic fertilizer comprises 10-15 pts. wt. Pleurotus ostreatus waste bacteria, 25-30 pts. wt. pig manure, 8-15 pts. wt. shiitake mushroom waste bacteria, 15-20 pts. wt. cow manure, 5-10 pts. wt. Flammulina velutipes waste bacteria, 10-15 pts. wt. sheep manure, 5-10 pts. wt. Pleurotus nebrodensis waste bacteria, 8-12 pts. wt. plant ash, 20-30 pts. wt. chicken manure and 5-10 pts. wt. trace element fertilizer.    USE - Waste mushroom organic fertilizer.    ADVANTAGE - The fertilizer improves crop yield, quality and taste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the manufacture of waste mushroom organic fertilizer comprising taking mushroom wastes, composting for 2-3 days, adding manure, mixing, drying, adding fermentation bacteria, mixing, fermenting for 40-50 days, adding plant ash and trace element fertilizer, mixing and granulating.
NOVELTY - Modifying palladium-gold catalyst comprises (a) after prior reduction of the initial supported palladium-gold catalyst removing palladium not bound to the palladium-gold alloy using nitric(V) acid, where the alloy is the active metal phase of the supported palladium-gold catalyst, and (b) reducing catalyst's metal active phase in flow of a hydrogen/argon reducing mixture to form modified supported palladium-gold catalyst. The atomic ratio of palladium and gold in the catalyst results from the gold/palladium is 1.44 before washing, and 1.5-2 after modification of the catalyst.    USE - The method is useful for modifying palladium-gold catalyst that is used for hydrodechlorination of tetrachloromethane (claimed).    ADVANTAGE - The method: provides palladium-gold catalyst having improved catalytic performance, 70% selectivity to hydrocarbons and poisoning resistance; allows palladium removal that does not results in removal of the alloy; and is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for palladium-gold catalyst obtained with the method comprising a suitable structure of the metal phase, in which palladium is contained exclusively in the catalyst's palladium-gold alloy, which means that the catalyst is free from palladium that is not bound to gold, and gold/palladium atomic ratio in modified supported palladium-gold catalyst is 1.5-2
NOVELTY - Nutrition soil preparation involves mixing sewage plant dehydrated sludge and fly ash in 1:0.7-1:1 mass ratio, and then performing aerobic fermentation to obtain the finished product.    USE - Method for preparing nutrition soil (claimed).    ADVANTAGE - The method enables to prepare nutrition soil in eco-friendly manner.
NOVELTY - The method involves mixing thiophosphoryl chloride, dichloromethane and n-butylamine, passing mixture into microchannel reactor via inlet and then allowing to react, feeding sodium hydroxide solution into reactor and then regulating back pressure using pressure valve, controlling reaction temperature of reactor using heat exchanger, cooling mixture, adding ammonia, separating gas and liquid from mixture and then separating inorganic layer and organic layer, cooling and crystallizing, and filtering crystallized product to obtain N-(n-butyl)thiophosphoric triamide.    USE - The method is useful for synthesizing N-(n-butyl) thiophosphoric triamide (claimed).    ADVANTAGE - The method is capable of easily synthesizing N-(n-butyl) thiophosphoric triamide with improved yield and reduced by-products in an economical and energy-efficient manner.    DETAILED DESCRIPTION - The method involves mixing thiophosphoryl chloride, dichloromethane and n-butylamine in a ratio of 1:0.5:2, passing the mixture into a microchannel reactor via an inlet and then allowing to react at 20-30 degrees C, preferably 25 degrees C for 20-30 seconds, preferably 20 seconds, feeding 10% sodium hydroxide solution into the reactor and then regulating back pressure to 0-0.5 MPa using a pressure valve, controlling the reaction temperature of the reactor using a heat exchanger, cooling the reaction mixture to 15 degrees C, adding ammonia to the reaction mixture, separating gas and liquid from the mixture using a gas-liquid separator and then separating inorganic layer and organic layer, cooling and crystallizing, and filtering crystallized product to obtain N-(n-butyl)thiophosphoric triamide.
NOVELTY - Preparing Lyophyllum decastes liquid culture medium involves weighing sucrose, soybean pulp, beef extract, magnesium sulfate heptahydrate, monopotassium phosphate and defoamer, mixing the weighed raw materials, adjusting pH to 5.5-6.5, adding the culture medium mixture into culture bottle, where each bottle comprises 400-500 parts mass culture medium, placing lid and packaging bottles, performing ozone sterilization for 1-2 hours after vacuumizing (50-80 KPa), and maintaining the bottles at 115 degrees C for 30 minutes, and then at 121 degrees C for 60 minutes.    USE - The method is useful for preparing L.decastes liquid culture medium (claimed).    ADVANTAGE - The method enables convenient preparation of inexpensive liquid culture medium, which enables rapid growth of L.decastes mushroom strain, improves efficiency and yield of the mushroom, and causes no pollution.    DETAILED DESCRIPTION - Method for preparing Lyophyllum decastes liquid culture medium involves weighing 10-30 parts mass sucrose, 2-5 parts mass soybean pulp, 1-3 parts mass beef extract, 0.3-1 part mass magnesium sulfate heptahydrate, 0.3-1 part mass monopotassium phosphate and 0.1-0.3 part mass defoamer, mixing the weighed raw materials, adjusting pH to 5.5-6.5, adding the culture medium mixture into culture bottle, where each bottle comprises 400-500 parts mass culture medium, placing lid and packaging bottles, placing the bottles in vacuum flask retorts, performing ozone sterilization for 1-2 hours after vacuumizing (50-80 KPa), and maintaining the bottles at 115 degrees C for 30 minutes, and then at 121 degrees C for 60 minutes.
NOVELTY - Plant insecticidal biofertilizer comprises biogas residue and is prepared by mixing biogas residues with water, adding straw powder, rice bran powder, and quicklime to mixture, uniformly mixing, piling and fermenting mixture using microbial inoculum, adding 19-30 %mass fermented biogas residues to 49-60 %mass soil, 5-10 %mass wood powder, 0.1-0.2 %mass trace elements fertilizer, and 15% mixture of tobacco powder and peat soil, mixing peat ash with palm, and adding yeast in a ratio of 7:1:2, mixing mixture for 4 hours and granulating mixture.    USE - As plant insecticidal biofertilizer.    ADVANTAGE - The biofertilizer is cost-effective, and environmentally-friendly.    DETAILED DESCRIPTION - Plant insecticidal biofertilizer comprises biogas residue and is prepared by mixing biogas residues with water in a ratio of 3:1, where moisture content of mixture is 10%, adding straw powder, rice bran powder, and quicklime to mixture in a ratio of 100:1:0.1, uniformly mixing, piling and fermenting mixture at 50-60 degrees C for 15-20 days using microbial inoculum, adding 19-30 %mass fermented biogas residues to 49-60 %mass soil, 5-10 %mass wood powder, 0.1-0.2 %mass trace elements fertilizer, and 15 %mass mixture of tobacco powder and peat soil, where the trace elements fertilizer is nitrogenous fertilizer, phosphate fertilizer and potassium fertilizer, mixing peat ash with palm, and adding yeast in a ratio of 7:1:2, mixing mixture for 4 hours and granulating mixture.
NOVELTY - Process for preparing water-soluble fertilizer, involves (a) adding 10 kg amino acids and 2 kg microbial inoculum to 20 kg fermented nutshell extract, and fermenting for 3 days, and (b) adding solid nitrogen, phosphorus, and potassium powder, 4% humic acid and trace elements into stirring tank, stirring, adding the product obtained in step (a), stirring for 10 minutes, transferring to granulation equipment, passing through 2-4 mm sieve, crushing, granulating, sieving, and packaging obtained product.    USE - The process is used for preparing water-soluble fertilizer in granule form (claimed).    ADVANTAGE - The prepared fertilizer has total nitrogen, phosphorus, and potassium content of 20%, and 8% trace elements, improves soil environment, increases nutrient absorption capacity of roots, adjusts soil pH, and promotes propagation of beneficial soil microflora.
NOVELTY - Preparing organic fertilizer by mixed fermentation of livestock manure and mushroom waste, involves (a) mixing sheep manure, mushroom waste and chicken manure, and adding fermentation bacteria, liquid fertilizer, and brown sugar solution, chopped fruit waste, juice of fruit waste or clear water, (b) stacking prepared mixture into a pile, covering the pile with plastic film and performing fermentation, and (c) decomposing fermented mixture, drying decomposed mixture, crushing dried product into particles having less than 2 mm diameter and dehydrating crushed particles.    USE - The method is useful for preparing organic fertilizer by performing mixed fermentation of livestock manure and mushroom waste (claimed).    ADVANTAGE - The organic fertilizer preparation method is simple.    DETAILED DESCRIPTION - Method for preparing organic fertilizer by mixed fermentation of livestock manure and mushroom waste, involves (a) mixing 50-70 %mass sheep manure, 15-35 %mass mushroom waste and 10-15 %mass chicken manure, adding 5-15 kg fermentation bacteria, 0-20 kg liquid fertilizer, and 15-25 kg brown sugar solution, chopped fruit waste, juice of fruit waste or clear water, and maintaining 35-45% moisture content, (b) stacking prepared mixture into a pile having 1.5-2.5 m width and 0.5-1.5 m height, covering the pile with plastic film and performing fermentation at 60-65 degrees C, and (c) decomposing fermented mixture, drying decomposed mixture, crushing dried product into particles having less than 2 mm diameter and dehydrating crushed particles, until the moisture content becomes less than 2%.
NOVELTY - Dragon fruit fertilizer comprises 12-14 pts. wt. potash fertilizer, 10-12 pts. wt. magnesium fertilizer, 40-60 pts. wt. chicken manure, 30-50 pts. wt. rabbit manure, 20-40 pts. wt. silkworm excrement, 20-40 pts. wt. donkey bone meal, 50-60 pts. wt. licorice, 40-50 pts. wt. bentonite, 30-40 pts. wt. weathered coal, 8-10 pts. wt. chitin, 20-40 pts. wt. middlings, and 140-160 pts. wt. water.    USE - As dragon fruit fertilizer.    ADVANTAGE - The fertilizer is harmless with respect to human.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) weighing the above-mentioned raw materials, and crushing weighed raw materials (except water), (b) adding water to crushed raw materials, and fermenting mixture for 4-6 days, and (c) granulating fermented material to obtain the product.
NOVELTY - Fertilizer comprises 80-100 pts. wt. chicken manure, 50-60 pts. wt. Achyranthes longifolia, 20-40 pts. wt. Sapindus mukorossi, 30-40 pts. wt. Eupatorium, 30-40 pts. wt. Medicago sativa, 8-10 pts. wt. phosphate solubilizing bacteria, 30-40 pts. wt. lotus root powder, 15-17 pts. wt. calcium nitrate, 18-22 pts. wt. radix bupleuri, 12-14 pts. wt. elecampane, 30-50 pts. wt. diatomite, and 220-260 pts. wt. water.    USE - The fertilizer is useful for Ligustrum lucidum leaves (claimed).    ADVANTAGE - The fertilizer is useful for improving nutrients in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing and uniformly mixing the above-mentioned raw materials, fermenting mixture for 2-4 days and granulating fermented product.
NOVELTY - Fertilizer is prepared by using 100 pts. wt. diatomite, 10-20 pts. wt. nitrogen, 8-15 pts. wt. phosphate, 6-10 pts. wt. potash, 5-10 pts. wt. humic acid, 1-3 pts. wt. Bacillus natto, 2-4 pts. wt. sodium chloride and 0.02-0.5 pt. wt. trace element.    USE - The fertilizer is useful for promoting growth of flowers.
NOVELTY - Fertilizer comprises 80-100 parts mass chicken manure, 70-90 parts mass pig manure, 100-120 parts mass mink manure, 60-80 parts mass weathered coal, 30-50 parts mass phosphate rock, 40-50 parts mass potassium mineral powder, 40-50 parts mass peat, 20-40 parts mass diatomite, 2-4 parts mass decomposing bacteria, 4-6 parts mass yeast, 3-5 parts mass photosynthetic bacteria and 300-360 parts mass water.    USE - The fertilizer is useful for Sagittaria sagittifolia (claimed).    ADVANTAGE - The fertilizer is easily decomposed and promotes growth of the S.sagittifolia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing the above-mentioned components except water, adding water to crushed components, sealing and fermenting obtained mixture, and drying fermented product.
NOVELTY - Method for preparing fertilizer for garden using bacterial residue, involves (a) mixing the bacterial residue, mushroom residual ash and rice bran in a ratio of (4-7):(1-2): (1.5-2), adding quicklime to obtained mixture for adjusting pH of the mixture to more than 9, and stacking the mixture, (b) subjecting the mixture to primary fermentation and secondary fermentation, where secondary fermentation is performed by (i) maintaining moisture content of primary fermented product at less than 40%, and (c) granulating and packaging obtained product.    USE - The method is useful for preparing fertilizer for garden (claimed).    ADVANTAGE - The method prepares fertilizer which is rich in nutritional components.    DETAILED DESCRIPTION - Method for preparing fertilizer for garden using bacterial residue, involves (a) mixing the bacterial residue, mushroom residual ash and rice bran in a ratio of (4-7):(1-2): (1.5-2), adding quicklime to obtained mixture for adjusting pH of the mixture to more than 9, and stacking the mixture, (b) subjecting the mixture to primary fermentation and secondary fermentation, where secondary fermentation is performed by (i) maintaining moisture content of primary fermented product at less than 40%, and (ii) using yeast at less than 50 degrees C, the secondary fermented product is maintained at less than or equal to 30%, the content of nitrogen, phosphorus and potassium of the secondary fermented product is greater than or equal to 5%, the content of organic matter of the secondary fermented product is greater than or equal to 45%, and the secondary fermented product has less than or equal to 0.1 mg/ml antibiotics, and (c) granulating and packaging obtained product.
NOVELTY - A nano-selenium bio organic-inorganic compound fertilizer contains 100-200 pts. wt. crop straw, 0.1-1.2 pt. wt. selenium dioxide, 100-300 pts. wt. animal waste, 300-800 pts. wt. sewage sludge, 150-350 pts. wt. urea, 70-200 pts. wt. mono- or di-ammonium phosphate, 100-300 pts. wt. potassium chloride, 50-100 pts. wt. silicon potash fertilizer, 0.1-5 pts. wt. cellulase enzyme, 0.2-6 pts. wt. Lactobacillus, 0.5-10 pts. wt. Candida utilis yeast, 0.2-8 pts. wt. Bacillus subtilis, 0.1-4 pts. wt. B. licheniformis and 1-10 pts. wt. borax.    USE - Nano-selenium bio organic-inorganic compound fertilizer (Claimed).    ADVANTAGE - The nano-selenium bio organic-inorganic compound fertilizer is economical, increases soil fertility, prevents soil compaction and improves the quality of crop. The nano-selenium compound fertilizer is manufactured by a simple process under mild reaction conditions, with improved productivity.    DETAILED DESCRIPTION - A nano-selenium bio organic-inorganic compound fertilizer comprises 100-200 pts. wt. crop straw, 0.1-1.2 pt. wt. selenium dioxide, 100-300 pts. wt. animal waste, 300-800 pts. wt. sewage sludge, 150-350 pts. wt. urea, 70-200 pts. wt. monoammonium phosphate or diammonium phosphate, 100-300 pts. wt. potassium chloride, 50-100 pts. wt. silicon potash fertilizer, 0.1-5 pts. wt. cellulase enzyme, 0.2-6 pts. wt. Lactobacillus, 0.5-10 pts. wt. Candida utilis yeast, 0.2-8 pts. wt. Bacillus subtilis, 0.1-4 pts. wt. B. licheniformis, 1-10 pts. wt. borax, 15 pts. wt. alkaline agent, preset amount of phosphoric acid and 1000-2000 pts. wt. water. An INDEPENDENT CLAIM is included for preparation of nano-selenium bio organic-inorganic compound fertilizer.
NOVELTY - Fertilizer comprises 5 pts. wt. lactic acid bacteria, 30-50 pts. wt. dried pig manure, 25-35 pts. wt. plant ash, 20-30 pts. wt. sugarcane bagasse, 30-40 pts. wt. traditional Chinese medicinal residue extract, 1-5 pts. wt. auxin, 2-8 pts. wt. zinc sulfate, 2-6 pts. wt. magnesium sulfate, 1-7 pts. wt. potassium dihydrogen phosphate, 0.2-0.8 pt. wt. ethephon, 0.1-0.5 pt. wt. rotenone, and 0.3-0.7 pt. wt. selenium yeast.    USE - As fertilizer for tomato (claimed).    ADVANTAGE - The fertilizer is nontoxic without side effects, and increases tomato yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) pulverizing dried pig manure plant ash, sugarcane bagasse and traditional Chinese medicinal residue, fermenting the pulverized mixture by adding purified water and lactic acid bacteria at 30-40 degrees C for 5-10 days, and (b) adding auxin, zinc sulfate, magnesium sulfate, potassium dihydrogen phosphate, ethephon, rotenone, and selenium yeast to the mixture, drying the mixture, and grinding the mixture.
NOVELTY - Fertilizer comprises 50-70 parts mass chicken manure, 60-80 parts mass peanut straw, 40-50 parts mass citric acid residue, 30-40 parts mass wheat bran, 20-30 parts mass radix sophorae flavescentis, 20-40 parts mass camphor leaves, 18-22 parts mass ryegrass, 3-5 parts mass microbe formulation, 17-19 parts mass calcium nitrate, 30-50 parts mass bentonite, 60-70 parts mass sawdust, and 250-270 parts mass water.    USE - As fertilizer for chestnut (claimed).    ADVANTAGE - The fertilizer is environmentally-friendly, and improves soil texture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding the above-mentioned materials into crusher, adding water, crushing the materials, sealing and fermenting crushed product for 4-6 days, adding fermentation product to granulator, and collecting granules.
NOVELTY - Vegetable fertilizer comprises 18-20 pts. wt. wheat straw, 15-17 pts. wt. soybean straw, 11-13 pts. wt. rice straw, 8-10 pts. wt. white gourd, 12-14 pts. wt. kudzu vine, 5-7 pts. wt. light carnallite powder, 6-8 pts. wt. slaked lime powder, 10-12 pts. wt. chelated zinc, 7-9 pts. wt. ammonium phosphate, 3-5 pts. wt. ectomycorrhizal root, 4-6 pts. wt. animal bone powder, 2-4 pts. wt. indole-3-butyric acid, 1-3 pts. wt. growth-promoting agent and 60-70 pts. wt. water.    USE - As vegetable fertilizer.    ADVANTAGE - The fertilizer is rich in nutrients, and environmentally-friendly, and improves tender taste of vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing and uniformly mixing the above-mentioned raw materials, fermenting mixture for 11 hours, and drying and granulating product.
NOVELTY - Fertilizer for Rubus corchorifolius comprises 28-30 pts. wt. corn straw, 23-25 pts. wt. wheat straw, 15-17 pts. wt. sesame straw, 10-12 pts. wt. Stylosanthes guianensis, 7-9 pts. wt. decomposing agent, 8-10 pts. wt. yeast, 15-17 pts. wt. ammonium sulfate, 12-14 pts. wt. potassium dihydrogen phosphate, 9-11 pts. wt. phosphate rock, 6-8 pts. wt. chelated zinc, 3-5 pts. wt. molybdenum disulfide, 2-4 pts. wt. tetramethyl glutaric acid and 60-80 pts. wt. water.    USE - The fertilizer is useful for promoting growth of R.orchorifolius.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) weighing the above-mentioned raw materials, crushing corn straw, wheat straw, sesame straw, and S.guianensis, and sieving crushed raw materials to 40 mesh sieve, (b) adding remaining raw materials to sieved material, mixing uniformly, fermenting mixture for 3.5 hours, and granulating fermented mixture to obtain the product.
NOVELTY - Fertilizer comprises 19-21 parts mass ammonium bicarbonate, 16-18 parts mass rock phosphate, 13-15 parts mass chicken manure, 7-9 parts mass potassium and magnesium salt, 11-13 parts mass diammonium phosphate, 14-16 parts mass photosynthetic bacteria, 3-5 parts mass copper carbonate, 4-6 parts mass soil conditioner, 7-9 parts mass chelated zinc, 1-3 parts mass manganese chloride, 2-4 parts mass humic acid, 5-7 parts mass farmyard manure, 6-8 parts mass soybean meal, 2-4 parts mass forchlorfenuron, and 40-50 parts mass water.    USE - As fertilizer for purple sweet potato (claimed).    ADVANTAGE - The fertilizer improves purple sweet potato yield, organic soil content, taste, nutritional content, flavor and appearance of purple sweet potato.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves stirring the above-mentioned components for 25 minutes to obtain mixture (A), allowing the mixture to stand, fermenting the mixture after sealing for 2 days, drying fermented mixture, and granulating dried mixture.
NOVELTY - Fertilizer is prepared using 8-10 pts. wt. nitrogen, 10-12 pts. wt. phosphate, 6-8 pts. wt. potash, 60-80 pts. wt. dried pig manure, 30-50 pts. wt. rice hull powder, 20-30 pts. wt. sea-tangle residue, 30-40 pts. wt. plant ash, 8-12 pts. wt. humic acid, 1-1.2 pts. wt. fungus powder, 0.3-0.5 pt. wt. effective microorganism (EM) agent, and 60-80 pts. wt. water.    USE - As fertilizer for tomato.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves weighing above-mentioned raw materials, crushing the weighed raw materials, fermenting the resulting powder for 5 days, and (d) granulating the fermented mixture to obtain product.
NOVELTY - Fertilizer for Brasenia schreberi comprises 60-70 pts. wt. sheep manure, 50-70 pts. wt. horse manure, 2-4 pts. wt. yeast, 30-40 pts. wt. cassava residue, 50-60 pts. wt. protein powder, 40-60 pts. wt. uronic residue, 30-50 pts. wt. tomato leaves, 40-50 pts. wt. cucumber, 30-40 pts. wt. balsam pear leaf, 20-30 pts. wt. red willow, 8-10 pts. wt. garlic, and 240-280 pts. wt. water.    USE - As fertilizer for B.schreberi.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing fertilizer, which involves (a) weighing the above-mentioned raw materials, crushing weighed raw materials using crusher, and stirring uniformly, and (b) fermenting mixture, drying fermented material, and crushing dried material to obtain the product.
NOVELTY - Method for preparing bioorganic fertilizer by steam explosion, involves (a) crushing tobacco straw, (b) adding crushed tobacco to steam explosion machine, and performing steam explosion, (c) adding cellulose-fermenting strains, nicotine-fermenting strains and lignin-fermenting strains to product obtained in step (b), then adding potassium and selenium functional strains, and uniformly mixing obtained mixture, (d) fermenting the mixture, and (e) adding nitrogen, phosphorus and potassium inorganic fertilizers to fermented product, and packing obtained product.    USE - The method is useful for preparing bioorganic fertilizer by steam explosion (claimed).    ADVANTAGE - The method consumes less time, and requires less space for fertilizer production.    DETAILED DESCRIPTION - Method for preparing bioorganic fertilizer by steam explosion, involves (a) crushing tobacco straw, (b) adding crushed tobacco to steam explosion machine, and performing steam explosion at 220-250 degrees C for 2-4 minutes, (c) adding cellulose-fermenting strains, nicotine-fermenting strains and lignin-fermenting strains to product obtained in step (b), then adding potassium and selenium functional strains, and uniformly mixing obtained mixture, (d) fermenting the mixture obtained in step (c), and (e) adding nitrogen, phosphorus and potassium inorganic fertilizers to fermented product, and uniformly mixing and packing obtained product.
NOVELTY - Fertilizer comprises 30-50 parts mass nitrogenous fertilizer, 80-100 parts mass pig manure, 60-80 parts mass chicken manure, 50-70 parts mass dairy manure, 30-40 parts mass weathered coal, 40-50 parts mass peat, 1.1-1.3 parts mass effective microorganism (EM) solution, 20-30 parts mass Alopecurus aequalis, 10-12 parts mass cassava residue, 20-30 parts mass river mud, 20-40 parts mass crabgrass and 120-140 parts mass water.    USE - The fertilizer is useful for Pennisetum (claimed).    ADVANTAGE - The fertilizer is prepared simply, and improves yield and quality of Pennisetum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing the above-mentioned components using crusher except water, adding water to crushed components, stirring obtained mixture, and granulating the mixture using granulator.
NOVELTY - Special fertilizer comprises 26-28 parts mass potassium nitrate, 21-23 parts mass farmyard manure, 20-22 parts mass calcium magnesium phosphate fertilizer, 18-20 parts mass urea, 15-17 parts mass rice straw, 12-14 parts mass wheat straw, 7-9 parts mass amino oligosaccharide, 5-7 parts mass microbial fertilizer, 2-4 parts mass Bacillus composition, 3-5 parts mass crop straw decomposed composition, 6-8 parts mass humic acid compound fertilizer, 2-5 parts mass boron residue, 1-3 parts mass zinc carbonate and 50-70 parts mass water.    USE - The special fertilizer is useful for sunflower (claimed).    ADVANTAGE - The fertilizer is rich in nutritional components and environmentally-friendly as it causes no pollution to environment, and improves soil fertility, and yield and quality of sunflower.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) crushing the rice straw and wheat straw using crusher to obtain powder having 40 mesh size, and (b) adding the potassium nitrate, farmyard manure, calcium magnesium phosphate fertilizer, urea, amino oligosaccharide, microbial fertilizer, Bacillus composition, crop straw decomposed composition, humic acid compound fertilizer, boron residue, zinc carbonate and water to the powder obtained in step (a), stirring obtained mixture, sealing and fermenting the mixture, and drying and bagging obtained product.
NOVELTY - Fertilizer comprises 40-50 wt.% rhizoma acori graminei extract, 20-25 wt.% sword bean extract, 10-15 wt.% chitosan, 3-5 wt.% titanium microsphere (120 nm), 3-5 wt.% basil essential oil, and 24-30 wt.% emulsifying agent.    USE - The fertilizer is useful for preventing downy mildew in lettuce (claimed).    ADVANTAGE - The fertilizer is nontoxic, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) weighing the above-mentioned raw materials, (b) obtaining rhizoma acori graminei, chopping, adding liquor, soaking at 52 degrees C for 7 days, and filtering solution to obtain rhizoma acori graminei extract, (c) mixing sword beans, brown sugar, and water in a ratio of 1:1.5:10, adding mixture into a glass jar, fermenting mixture at 25-30 degrees C for 7 days, and filtering fermented product to obtain sword bean extract, (d) mixing extracts obtained in steps (b) and (c), adding chitosan, titanium microsphere, and basil essential oil, and mixing uniformly at 40 degrees C for 10 minutes, and (e) adding emulsifying agent to mixture obtained in step (d), and mixing uniformly to obtain the product.
NOVELTY - Adsorbent composition comprises 0.5-5 pts. wt. water hyacinth, 1-10 pts. wt. bagasse, 0.2-3 pts. wt. lignite and 0.2-3 pts. wt. biogas residue.    USE - As adsorbent composition for fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the adsorbent composition, which involves (a) drying water hyacinth, bagasse and biogas residue at 100 degrees C for 12-24 hours, (b) crushing resulting mixture to obtain 60 mesh size powder, (c) mixing the powder with binder and water to obtain paste, and (d) adding lignite to the paste, drying the mixture at 100 degrees C for 12 hours in an oven, and crushing the dried mixture to obtain product.
NOVELTY - Adsorbent is prepared using 10-35 pts. wt. bagasse, 18-32 pts. wt. carbonized tobacco stem and 1-9 pts. wt. peat.    USE - As adsorbent for microbial fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the adsorbent, which involves (a) drying bagasse and peat at 100 degrees C for 12-24 hours, (b) crushing the resulting dried mixture to obtain 60 mesh size powder, (c) subjecting the tobacco stem to carbonization at 550-600 degrees C, (d) mixing the resulting product obtained in the step (b) and (c) with binder and water, (e) homogenizing the resulting mixture, drying the homogenate at 100 degrees C for 12 hours, and crushing the dried mixture to obtain product.
NOVELTY - Fertilizer comprises 80-100 pts. mass rabbit dung, 40-60 pts. mass pig manure, 40-50 pts. mass ryegrass, 30-40 pts. mass licorice powder, 5-7 pts. mass chitin, 60-80 pts. mass kaolin, 20-40 pts. mass soybean curb residue, 30-50 pts. mass wheat bran, 18-20 pts. mass wintergreen oil, 2-4 pts. mass photosynthetic bacteria, 8-10 pts. mass Lotus root starch, and 150-160 pts. mass water.    USE - As fertilizer for safflower (claimed).    ADVANTAGE - The fertilizer is rich in nutrients, and prepared simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves mixing the above-mentioned raw materials, adding 150-160 pts. mass water, stirring and sealing the mixture, fermenting the sealed mixture for 4-6 days, standing the fermented mixture for 20 hours, and granulating the fermented mixture.
NOVELTY - Fertilizer comprises 80-100 parts mass pig manure, 20-40 parts mass oil residue, 40-60 parts mass plant ash, 20-30 parts mass phosphate mineral powder, 18-22 parts mass potassium mineral powder, 40-50 parts mass flour, 30-40 parts mass Phellodendron, 20-40 parts mass pine needle, 8-10 parts mass radix isatidis, 3-5 parts mass culture powder of bacteria, 30-50 parts mass bentonite, and 170-190 parts mass water.    USE - As fertilizer for Kalanchoe blossfeldiana (claimed). The fertilizer is useful for improving fertility of soil.    ADVANTAGE - The fertilizer is rich in nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding the above-mentioned materials into crusher, adding water, crushing the materials, sealing and fermenting crushed product for 4-6 days, adding fermentation product to granulator, and collecting granules.
NOVELTY - Special fertilizer comprises 20-22 pts. wt. urea, 18-20 pts. wt. prepared pig manure, 10-12 pts. wt. plant ash, 3-5 pts. wt. potassium humate, 15-17 pts. wt. potassium dihydrogen phosphate, 12-14 pts. wt. ferrous sulfate, 11-13 pts. wt. cuprous oxide, 7-9 pts. wt. green manure, 6-8 pts. wt. manganese sulfate, 2-4 pts. wt. microbial fertilizer, 1-3 pts. wt. ammonium molybdate, 4-6 pts. wt. omethoate, 1-2 pts. wt. Rhizobium, 2-4 pts. wt. Cycocel (RTM: Plant growth regulant) and 60-70 pts. wt. water.    USE - As special fertilizer for mung beans.    ADVANTAGE - The fertilizer promotes root growth, increases pod number, yield and quality, and prevents plant lodging.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned materials, and stirring the mixture uniformly for 12 minutes.
NOVELTY - Fertilizer comprises 10-30 pts. wt. sheep manure, 10-30 pts. wt. chicken manure, 5-10 pts. wt. plant ash, 5-15 pts. wt. urea, 5-20 pts. wt. calcium superphosphate, 1-10 pts. wt. ammonium sulfate, 1-10 pts. wt. potassium sulfate, 10-15 pts. wt. diammonium phosphate, 1-10 pts. wt. clove leaves, and 0.01-0.1 pt. wt. Bacillus thuringiensis.    USE - The fertilizer is useful for protecting golden Camellia from insect pests (claimed).    ADVANTAGE - The fertilizer is rich in nutrients and environmentally-friendly, causes minimal toxicity, and does not influence quality of Camellia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding 3-10 times water to the clove leaves, performing extraction, filtering extract, uniformly mixing B.thuringiensis and extract, drying mixture, crushing dried material to obtain product having particle size of 10-120 meshes, and adding and mixing additive and remaining raw materials to the product to obtain the fertilizer.
NOVELTY - Organic fertilizer comprises 0.7-1.5 pts. wt. soybean pulp, 1.5-2 pts. wt. grain bran, 1.3-1.5 pts. wt. seaweed, 1-1.5 pts. wt. silkworm excrement and 4-5 pts. wt. glucose.    USE - The organic fertilizer is useful for peach (claimed).    ADVANTAGE - The organic fertilizer is cost-effective, rich in nutrients and easy to obtain, and increases yield of the peach.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves crushing the above-mentioned raw materials (except glucose), adding mixture into reaction vessel, adding 10-15 times hot water to the reaction vessel, soaking mixture for 6-8 hours, fermenting mixture at 55-65 degrees C for 8-10 hours, adding glucose to the mixture, heating mixture at 50-60 degrees C and cooling obtained product.
NOVELTY - Manufacture of electrochemical cell involves providing support, forming electrolyte on support, heat-treating in atmosphere containing mixture of hydrogen, inert gas and methane gas, forming cathode on upper surface of coated electrolyte, and heat-treating in atmosphere containing inert gas.    USE - Manufacture of electrochemical cell used as fuel cell, electrolytic cell and oxygen separation module (all claimed).    ADVANTAGE - The method provides electrochemical cell having excellent electroconductivity, crack resistance, and long-term stability.
NOVELTY - Phenyl(pyridin-2-yl)methanol as raw material, ionic hydride as catalyst, and dry air or dry oxygen as oxidant are reacted at 0-30 degrees C, to obtain 2-benzoylpyridine.    USE - Oxidation-synthesis of 2-benzoylpyridine (claimed).    ADVANTAGE - The method enables environmentally-friendly oxidation-synthesis of 2-benzoylpyridine with yield of 95% or less under mild reaction conditions, by simple method.
NOVELTY - Fertilizer comprises 10-15 pts. wt. sodium nitrophenolate, 10-15 pts. wt. sodium alpha -naphthyl acetate, 13-25 pts. wt. chlormequat, 12-20 pts. wt. boric acid, 12-21 pts. wt. humic acid, 11-32 pts. wt. 2,4-dinitrophenol or its sodium salt, 11-30 pts. wt. tea polyphenol or its sodium salt, 11-30 pts. wt. p-nitrophenol or its sodium salt, 11-20 pts. wt. dodecylbenzene sulfonic acid or its sodium salt, 15-20 pts. wt. polyaspartic acid, 13-20 pts. wt. triiodobenzoic acid, 10-26 pts. wt. nitrogen-fixing bacterium, and 10-12 pts. wt. synergistic additive.    USE - The fertilizer is useful for promoting growth of plants, fruits and vegetables.    ADVANTAGE - The fertilizer exhibits synergistic effect. The method is simple and cost-effective, and consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) placing sodium nitrophenolate, sodium alpha -naphthyl acetate, chlormequat, boric acid, humic acid, 2,4-dinitrophenol or its sodium salt, tea polyphenol or its sodium salt, p-nitrophenol or its sodium salt, and dodecylbenzene sulfonic acid or its sodium salt in a vessel, and applying a pressure of -0.5 MPa to -0.2 MPa, and temperature of 50-60 degrees C to the vessel, (b) mixing polyaspartic acid, triiodobenzoic acid, and nitrogen-fixing bacterium for 30-40 minutes, dissolving peptide, alkylsulfonyl chloride, octadecylamine, polyether triol, aluminum sulfate, and polypropylene glycol at 30-40 degrees C, (c) filtering the dissolved solution through a membrane having pore size of 2-3 mm to obtain filtrate, and drying the filtrate at 180-220 degrees C for 2-3 hours, (d) dry granulating the dried filtrate to obtain granules having particle diameter of 4-6 mm, and (e) spraying 20-30% coating liquid on the granules placed in a coating chamber, where the chamber temperature is maintained at 49-55 degrees C.
NOVELTY - Use of microorganism microbial inoculum for treating petrochemical sewage sludge, is claimed.    USE - Microorganism microbial inoculum for treating petrochemical sewage sludge.
NOVELTY - A biomass molding fuel tar creosote content improving method involves carrying out pyrolysis of biomass molding fuel under an alkaline air atmosphere comprising ammonia gas and air in a volume ratio of 1-3: 100 to obtain biomass molding active carbon and tar byproduct.    USE - Method for improving creosote content in biomass molding fuel tar.    ADVANTAGE - The method enables effectively improving creosote content in biomass molding fuel tar from less than 80 wt.% to 85-92 wt.%, reducing environmental pollution caused by the tar byproduct, reducing preparing cost of the phenolic resin adhesive and increasing the substitution ratio of the tar byproduct in the reaction of substituting part of phenol, thus improving production of phenolic resin adhesive from 25% to 30-50%.
NOVELTY - A purified Bdellovibrio bacteriovorus separating method involves taking municipal sewage as sludge sample after separating and screening the Gram-negative germ, carrying out liquid proliferation and centrifugal separating process to obtain host suspension, processing the sludge to obtain precipitate, purifying the liquid by using nutrition broth double-layer agar plate dilution method to obtain mixed suspension, followed by diluting the suspension with nutrition meat soup culture liquid and culturing to separate Bdellovibrio bacteriovorus suspension.    USE - Method for separating purified Bdellovibrio bacteriovorus from activated sludge.    DETAILED DESCRIPTION - A purified Bdellovibrio bacteriovorus separating method involves taking municipal sewage treatment plant sedimentation of activated sludge as sludge sample after separating and screening the Gram-negative germ, carrying out liquid proliferation for 18-24 hours and centrifugal separating process with phosphate buffer solution at 4 degrees C to obtain host suspension, processing the sludge at 4-10 degrees C to speed of 800-1000 rpm for 20-30 minutes to obtain precipitate, adding the precipitate with sterile phosphate buffer solution to obtain the re-suspending liquid as Bdellovibrio bacteriovorus source liquid, purifying the liquid by using nutrition broth double-layer agar plate dilution method at 25-30 degrees C for 3 days to obtain mixed suspension, followed by diluting the suspension with 0.5-1% nutrition meat soup culture liquid at 25-30 degrees C and culturing for 3 days to separate Bdellovibrio bacteriovorus suspension.
NOVELTY - Preparing 17-ethynyl-androsta-4,16-diene-3-one derivatives (II) comprises reacting 17 alpha -ethynyl-androsta-4-ene-3-one 17 beta -nitrate derivatives (I) in presence of a monovalent silver or copper salt catalyst and an aprotic organic solvent, where the reaction temperature is 25 degrees C to reflux temperature of the solvent.    USE - The method is useful for preparing 17-ethynyl-androsta-4,16-diene-3-one derivatives (claimed).    DETAILED DESCRIPTION - Preparing 17-ethynyl-androsta-4,16-diene-3-one derivatives of formula (II) comprises reacting 17 alpha -ethynyl-androsta-4-ene-3-one 17 beta -nitrate derivatives of formula (I) in presence of a monovalent silver or copper salt catalyst and an aprotic organic solvent, where the reaction temperature is 25 degrees C to reflux temperature of the solvent.    Dotted bond = single or double bond; and    R = H, alpha -CH3, alpha -F or beta -F.
NOVELTY - The electrolyzer (10) has a protection sheet element (44) that is provided between electrolytic membrane (38) and anode electric power feeding structure (40). Through-hole (44a) is set to an aperture diameter smaller than largest aperture diameter of anode electric power feeding structure. The higher pressure hydrogen is generated to a cathode side. An anode catalyst layer (40a) is provided to cover inner wall face of through-hole of protection sheet element and is provided in contact portion of protection sheet element and electrolytic membrane.    USE - Differential pressure type high-pressure water electrolyzer for generating oxygen and hydrogen, in unit cell.    ADVANTAGE - The solid polymer electrolyte membrane is entrapped in the through-hole of protection sheet element, so as to suppress lacking of anode catalyst. The high electric current flowing through polymer electrolyte membrane is prevented reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the unit cell.    Differential pressure type high-pressure water electrolyzer (10)    Solid polymer electrolyte membrane (38)    Anode electric power feeding structure (40)    Anode catalyst layer (40a)    Protection sheet element (44)    Through-hole (44a)
NOVELTY - A system comprises extraction component which extracts hydrogen from source of water, and energy component which harnesses energy from renewable energy source using extracted hydrogen.    USE - A system for sustainable economic development process (claimed).    ADVANTAGE - System has low capital, maintenance and fuel costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sustainable economic development process which involves dissociating greater than or equal to 2 substances from feedstock by providing energy from renewable energy source to assist in performing the dissociation and extracting hydrogen from greater than or equal to 2 dissociated substances using renewable energy source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ocean-based system of integrated production of sustainable economic development.
NOVELTY - The apparatus (100) has a pressing mechanism (102), which presses a cell unit (12,14) in the stacking direction. The pressing mechanism has first (62,104), second (68) and third corrosion-resistant members (80) and pressure-resistant member (84). The third corrosion-resistant member covers each outer peripheral portion of first and second corrosion-resistant members to form a fluid introduction chamber (82). The pressure-resistant member is arranged on the outer peripheral portion of third corrosion-resistant member and holds the pressure in the fluid introduction chamber.    USE - Differential pressure water electrolysis apparatus for producing hydrogen used as fuel gas for generating electric power in fuel cell.    ADVANTAGE - Machining cost is reduced, and assembly workability is improved. Structure is simplified, and desired corrosion resistant function and pressure-resistant function are retained with a lightweight and economic configuration. Amount of high-cost corrosion-resistant material used is minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the main portion of a differential pressure type high-pressure water electrolysis apparatus.    Cell units (12,14)    First corrosion-resistant members (62,104)    Second corrosion-resistant member (68)    Third corrosion-resistant member (80)    Fluid introduction chamber (82)    Pressure-resistant member (84)    Differential pressure water electrolysis apparatus (100)    Pressing mechanism (102)
NOVELTY - Growing a microbial organism comprises dispersing an amount of the thermally treated lignocellulosic biomass into an amount of a carrier liquid to create a slurry; contacting the slurry with an enzyme under hydrolysis conditions of a carbohydrate component of the slurry, to produce a hydrolyzed composition comprising simple sugar or sugars derived from the xylans and glucans of the thermally treated biomass; and cultivating the microbial organism in a cultivation environment comprising a portion of the hydrolyzed composition.    USE - The method is used for growing a microbial organism (claimed).    ADVANTAGE - Provided is an inexpensive method for growing a microbial organism by using hydrolyzates of lignocellulosic feedstocks containing low inhibiting effects.    DETAILED DESCRIPTION - Growing a microbial organism comprises (a) thermally treating a lignocellulosic biomass feedstock to create a thermally treated lignocellulosic biomass, the thermally treated lignocellulosic biomass comprising xylans, glucans and lignin; (b) dispersing an amount of the thermally treated lignocellulosic biomass into an amount of a carrier liquid to create a slurry; (c) contacting the slurry with an enzyme under hydrolysis conditions of a carbohydrate component of the slurry, to produce a hydrolyzed composition comprising simple sugar or sugars derived from the xylans and glucans of the thermally treated biomass, where the simple sugar or sugars can be metabolized by the microbial organism; and (d) cultivating the microbial organism in a cultivation environment comprising a portion of the hydrolyzed composition under conditions and for a cultivation time sufficient to grow the microbial organism.
NOVELTY - Fermentable sugars are prepared from biomass resources by pretreating biomass with dilute acid, neutralizing pretreated biomass with acid-neutralizing neutralizers, separating pentose sugars from pretreated biomass to obtain pretreated biomass slurry, and hydrolyzing biomass slurry.    USE - Preparation of fermentable sugars from biomass resources (claimed).    ADVANTAGE - The process is environment-friendly and low cost while producing high yield of fermentable sugars.
NOVELTY - Device comprises a flat tube system (2) comprising tubes arranged in a vertical plane to light transmitting material, an inlet of the tube system with a pump (7) in its lower region for supplying sewage, a settling tank (4) for discharging sewage stream (3) from the tube system in the upper region. The settling tank is provided with an outlet (5), arranged in the lower region of the tube system, from which the water enriched with algae is acted upon by sunlight by the passage through the tube system.    USE - The device is useful for photosynthetic production of microalgal biomass from a sewage (claimed).    ADVANTAGE - The device: achieves mass production of algae; and allows cost efficient harvesting of biomass.    DETAILED DESCRIPTION - Device for photosynthetic production of microalgal biomass from a sewage, comprises a flat tube system (2) comprising tubes arranged in a vertical plane to light transmitting material, an inlet of the tube system with a pump (7) in its lower region for supplying sewage, a settling tank (4) for discharging sewage stream (3) from the tube system in the upper region. The settling tank is provided with an outlet (5), arranged in the lower region of the tube system, from which the water enriched with algae is acted upon by sunlight by the passage through the tube system. The water recirculating is optionally transferred to the inlet of the tube system or is dissipated at a sufficient enrichment for the harvesting the algae obtained at an additional extraction point.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of removal of the settling algae mixed population.    Tube system (2)    Sewage stream (3)    Settling tank (4)    Outlet (5)    Pump (7)
NOVELTY - Extraction of Eucalyptus leaves flavonoid comprises picking Eucalyptus leaves, washing with water, drying, and crushing; adding immobilized enzyme, adding into extraction vessel, and supercritical carbon dioxide extracting; and vacuum-separating.    USE - Method for extraction of Eucalyptus leaves flavonoid (claimed).    ADVANTAGE - The method has low organic solvent residue, recyclable immobilized enzyme, high extraction time and flavonoid yield of 2.32-3.85%, and no environmental pollution.    DETAILED DESCRIPTION - Extraction of Eucalyptus leaves flavonoid comprises (A) picking Eucalyptus leaves, washing with water, drying to 60-100 degrees C until moisture content is less than 3%, and crushing into 60-100 mesh powder; (B) adding immobilized enzyme at ratio of 20-100:1, adding into extraction vessel, and supercritical carbon dioxide extracting to 50-75 degrees C at 25-45 MPa and at supercritical carbon dioxide flow rate of 25-50 kg/hour for 2-3 hours; and (C) vacuum-separating to 40-50 degrees C at 5-10 MPa and to 30-40 degrees C at 4-5 MPa. The immobilized enzyme is cellulase, xylanase, pectinase, hemicellulase and/or snailase.
NOVELTY - A magnesium-based metal organic framework comprises metal ion compound and organic ligand in complex framework structure. The metal ion is magnesium(II) ion, nickel (II) ion, copper(II) ion, zinc(II) ion, cobalt(II) ion, and/or calcium(II) ion. The organic ligand is carboxylic acid, monohalomethyl or its derivatives, or polyhalogenated compound.    USE - Magnesium-based metal organic framework used for absorbing and separating methane-nitrogen mixed gas (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of magnesium-based metal organic framework comprising dissolving metal compound and organic ligand into solvent, adding coordination agent, and uniformly stirring at room temperature; reacting; and separating solid, washing, drying, and activating.
NOVELTY - Sludge and organic wastes deodorizing and decomposing agent comprises activated matrix and liquid solution. The activated matrix comprises 0.1-1 wt.% rice bran, soybean powder, bagasse powder and bitter tea powder, 0.1-1 wt.% rice wine, 0.1-1 wt.% rice vinegar, 0.5-10 wt.% molasses, and 0.001-0.1 wt.% iron, aluminum, magnesium and/or silicon. The liquid solution is water solution comprising lactic acid bacteria, microzyme, yeast and bacteria.    USE - Sludge and organic wastes deodorizing and decomposing agent.    ADVANTAGE - The agent eliminates sludge smell and adhesive-like substance to improve dehydration rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the application of sludge and organic wastes deodorizing and decomposing agent comprising mixing sludge and organic wastes deodorizing and decomposing agent and 20-300 times diluted aqueous solution, stirring and applying into sludge spill or organic waste heap.
NOVELTY - Hydrogen preparation involves taking ammonia as raw material, where cathode and anode are inserted in electrolyte-containing ammonia. The applied voltage is of 0.6-0.8 Volt. Electrolysis reaction is performed at 50-60 degrees C generating hydrogen at cathode.    USE - Method for preparing hydrogen (claimed).    ADVANTAGE - The method enables to prepare hydrogen in a cost-effective manner.
NOVELTY - Hydrogen oxygen generator comprises a housing (1), a fixing plate (3), a lower shell, an electrode group (5), a guide hole (6) and a guide cylinder (7) and an upper shell, where the fixing plate is connected to the lower shell. The electrode group is provided in the lower shell, the guide hole is provided in the fixing plate. The guide cylinder is provided in the upper shell body. The electrode group is provided for performing electrolysis in the lower shell for producing metallic titanium by inserting hydrogen and oxygen through the air guide hole.    USE - Hydrogen oxygen generator. .    ADVANTAGE - The hydrogen oxygen generator is durable, easily disassembled and cleaned.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a hydrogen oxygen generator.    Housing (1)    Fixing plate (3)    Electrode group (5)    Guide hole (6)    Guide cylinder (7)
NOVELTY - The device has a loading line supplied with an automatic bunker. A magnetic separator is made with purification of waste from metallic inclusions and connected with four helical conveyers by three screw unloaders. The loading line is connected with a gas generator by gravity pipes and supplied with a generator gas withdrawal line. The generator gas withdrawal line contains an air-cooled passage, a vortex trap, cooling heat exchangers, scrubbers, a bag-type filter and a fine purification filter. The generator gas withdrawal line is connected to a fuel supply line.    USE - Device for utilization of organic waste.
NOVELTY - This utility model provides a continuous producing biogas, without pollute, resource use rate v of continuous producing biogas collection system, it comprises a water inlet end through IC reactor, pneuma liquid separating tank, an air storage tank water inlet pipe and sewage source a is connected, liquid collection pool, also has pump is equipped with a water inlet end of the IC reactor; a has air inlet and air outlet is set up in the tank, and also has the pneuma valve set at the air outlet of the pneuma storage tank, the air outlet end of the IC reactor through the collection tube and the pneuma liquid separation tank of a corresponding connected air inlet and outlet the pneuma liquid separation tank is a through by gas pipe and the storage tank.
NOVELTY - The device has a second tubular electrode (200) which is arranged coaxially relative to the first tubular electrode (100). First or second tubular electrode is configured as a cathode and the other is configured as an anode. Inner cross-sectional area of the first tubular electrode is greater than the outer cross-sectional area of the second tubular electrode. Second tubular electrode has orifices, in which orifices (208) are adapted for producing a first gas stream that is enriched with a first gas within the inner space or the external space of the second tubular electrode.    USE - Electrochemical device for producing fluid electrolytic decomposition-based gas.    ADVANTAGE - Reduces unheard of low concentration of potassium hydroxide in electrolyte solution significantly, and eliminates danger to human and environment due to a possible leakage of electrolyte solution by using adequate electrodes to avoid unwanted reactions which can produce impurities in the hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of an electrolytic device.    First tubular electrode (100)    Electric connectors (110,220)    Second tubular electrode (200)    Orifices (208)
NOVELTY - Manufacture of substituted urea (I) and carbamate compound (II) or (III) involves reacting amine compound (IV), alkylene oxide compound (V) or (VI), and carbon dioxide in the presence of an indium-containing ionic liquid-based catalyst system comprising indium-alkali metal-containing composite catalyst system (VII) containing indium-containing complex (VIII) as main catalyst and alkali metal halide (IX) as additive.    USE - Manufacture of substituted urea and carbamate compound used as precursor of polyurethane and raw material or intermediate material for production of agrochemicals, herbicides, and insecticides.    ADVANTAGE - The method enables efficient manufacture of substituted urea and carbamate compound with high yield and efficient recycling of catalyst, by simple and economical process, which provides polyurethane with excellent physicochemical characteristics and reduced yellowing property.    DETAILED DESCRIPTION - Manufacture of substituted urea of formula (I) and carbamate compound of formula (II) or (III) involves reacting amine compound of formula: R1-NH2 (IV), alkylene oxide compound of formula (V) or (VI), and carbon dioxide in the presence of an indium-containing ionic liquid-based catalyst system comprising indium-alkali metal-containing composite catalyst system of formula: (Q) (InX4-nY'n)-MZ (VII) containing indium-containing complex of formula: (Q) (InX4-nY'n) (VIII) as main catalyst and alkali metal halide of formula: MZ (IX) as additive.    (Q)=cation of ionic liquid;    (InX4-nY'n)=anion of ionic liquid;    MZ=alkali metal halide;    Q=imidazolyl, phosphonyl, ammonium, or pyridinyl;    X,Z=chloro, bromo, or iodo;    Y'=chloro or bromo;    M=alkali metal;    n=0-3;    R1=2-10C aliphatic alkyl, 4-10C alicyclic alkyl, or 5-6C aryl (all optionally substituted by hydroxy, acyl, carboxy, halo, or -NH2);    R2=2-10C aliphatic alkyl, 4-10C alicyclic alkyl, 5-6C aryl, or halo;and    n'=1-5.
NOVELTY - The device has a reactor (1) provided with a chamber (2). Exhaust gases are heated from combustion of torrefaction in a cyclone chamber (21) of a burner (22). A pump (42) is connected to a feeding screw (33). Exhaust outlets (8, 9) in a side wall (5) are respectively connected to a chimney (52) via channels (38, 40) and outlets (39, 41). A stack and a conveyor (35) are respectively provided with thermocouples (49) and an automatic gas analyzer (51). The cyclone chamber is supplied with air.    USE - Device for performing autothermal valorisation of biomass or organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a device for performing autothermal valorisation of biomass or organic waste.    Reactor (1)    Chamber (2)    Side wall (5)    Exhaust outlets (8, 9)    Cyclone chamber (21)    Burner (22)    Feeding screw (33)    Conveyor (35)    Channels (38, 40)    Outlets (39, 41)    Pump (42)    Thermocouples (49)    Automatic gas analyzer (51)    Chimney (52)
NOVELTY - This utility model bracket claims an energy-saving environment-friendly chicken cultivating greenhouse, belongs to a technology field of chicken, the technology point comprises body, solar energy solar panels, marsh gas system, storage battery, an exhaust fan, a cooling spray head, excrement cleaning water pipe, water pump and ozone deodorizer, wherein comprises side wall and a body part in a shed roof, a shed body also has mounting bracket, a fill light mounted in a holder, a solar energy solar panels mounted a top, an exhaust fan mounted in the side wall, a cooling spray head mounted at a part in a shed body, the ozone deodorizer mounting a cooling spray head is up, the excrement cleaning water pipe adhesive b shed body bottom installation, the marsh gas system comprises marsh gas pool, marsh gas storage tank, a marsh gas generator and biogas residue pump. The energy-saving environment-friendly chicken cultivating greenhouse structure is simple, the cost is low, a semi automatic, which greatly reduces the labour intensity, using marsh gas power generation and solar energy power generation, energy-saving and environment-friendly, at the same time reduce the generating of a plague.
NOVELTY - Methanation catalyst of natural iron ore-nickel is claimed. The catalyst carrier is precalcined natural iron ore molded body, the content of the nickel oxide in nickel loaded catalyst is 2-15 wt.%, the mass ratio of nickel and iron in catalyst is 0.03:1-20:1.    USE - Used as methanation catalyst of natural iron ore-nickel.    ADVANTAGE - The catalyst has high activity, good stability and high strength. The method has simple preparation process, uses economical and easily available raw material, is economical and environmentally friendly, is suitable for coal-based and biomass-based synthetic gas multi-H/C condition carbon dioxide/carbon monoxide methanation process, especially in fixed bed methanation operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing catalyst comprising (i) pre-sintering iron-containing natural ore or aluminate cement powder at 500-1300 degrees C for 1-5 hours, smashing iron-containing natural ore to small diameter of 75 mu m, with diameter less than 75 mu m aluminate cement powder and diameter less than 10 mu m graphite or carbon powder, mixing, adding deionized water and stirring, molding, curing, preparing molded body, where the molded body comprises 40-90 wt.% iron-containing natural ore powder, 5-30 wt.% aluminate cement powder, 0-10 wt.% graphite or carbon powder and 5-20 wt.% deionized water, (ii) sintering obtained molded body at 500-1300 degrees C for 5 hours, cooling to room temperature to obtain molding, and (iii) preparing nickel salt aqueous solution with cation concentration of 0.1-8 mol/l, using impregnation method, mixing nickel salt aqueous solution and step (ii) prepared carrier, dipping and absorbing, drying, and baking to obtain the needed supported catalyst.
NOVELTY - A selenoprotein is extracted from selenium-enriched tea leaves by crushing selenium-enriched tea leaves, sieving through 80-100 mesh sieve to obtain selenium-enriched tea powder, removing polyphenol, drying, crushing, sieving through 80-100 mesh sieve to obtain substance (A), adding 1 g substance (A) into 30-70 ml sodium hydroxide solution, placing in water bath, heating at 70-90 degrees C for 3-4 hours, centrifuging to obtain supernatant, adjusting pH to 2.5-3.5, standing, centrifuging to obtain precipitate, and drying.    USE - Extraction of selenoprotein from selenium-enriched tea leaves (claimed).    ADVANTAGE - Extraction process is simple, easy, and environment-friendly.
NOVELTY - The device has a flocculation unit (4) connected with a liquid hose (7) through a sedimentation pool (8). A lower part of the flocculation unit is connected with an algae flocculating agent and stirring device (3). The sedimentation pool is connected with a sedimentation pool definition hose (11-1). Bottom of the sedimentation pool is connected with a sedimentation pool precipitate hose (11-2). A sample tube (12) is connected with a tube centrifuge machine (13). A liquid flocculating agent and stirring device is connected with an electric source controller (15).    USE - Large scale mico-algae biomass cascade efficient energy-saving harvesting device.    ADVANTAGE - The device increases sample flow speed and amplification production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a large scale mico-algae biomass cascade efficient energy-saving harvesting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a large scale mico-algae biomass cascade efficient energy-saving harvesting device.    Algae flocculating agent and stirring device (3)    Flocculation unit (4)    Liquid hose (7)    Sedimentation pool (8)    Sedimentation pool definition hose (11-1)    Sedimentation pool precipitate hose (11-2)    Sample tube (12)    Tube centrifuge machine (13)    Electric source controller (15)
NOVELTY - Method for performing anaerobic fermentation of sludge, involves performing nitrite pretreatment, increasing organic material in the sludge, mixing materials, adjusting pH value of mixture to alkaline condition, performing alkaline digestion to further promote process of anaerobic fermentation, performing hydrolysis to enhance accumulation of short-chain fatty acids while suppressing activity of methanogenic microorganisms, and improving yield of short-chain fatty acids.    USE - The method for performing anaerobic fermentation of sludge to produce short-chain fatty acids (claimed).    ADVANTAGE - The method improves yield of short-chain fatty acids, and utilizes waste sludge.
NOVELTY - A F85-20 protein comprising: (a) fully defined 462 amino acids (SEQ ID NO. 2) given in the specification; and (b) amino acid sequence of (a) having one or more amino acid residues that are substituted, deleted, and/or added, and comprises the same function of (a), is new.    USE - The F85-20 protein, DNA molecule, recombinant vector, recombinant bacterium, or transgenic cell line is useful for preparing beta-glucosidase, cellulase, or xylanase, where the enzyme has optimum pH value of 6.0, and optimum temperature of 65 degrees C; and for degradation of biomass, preferably corn biomass (all claimed).    ADVANTAGE - The F85-20 protein can retain activity of 70% or 80% at optimum conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a DNA molecule encoding the F85-20 protein;    (2) a recombinant vector, recombinant bacteria, and transgenic cell line comprising the DNA molecule; and    (3) a method for preparing beta-glucosidase, cellulase, or xylanase, comprising fermenting the recombinant strain.
NOVELTY - Fertilizer composition comprises 40-60 pts. wt. rabbit dung, 30-40 pts. wt. horse dung, 30-50 pts. wt. peanut cake, 20-40 pts. wt. monoammonium phosphate, 40-60 pts. wt. calcium powder, 18-22 pts. wt. lard residue, 20-30 pts. wt. furfural residue, 60-80 pts. wt. wooden meal, 40-50 pts. wt. Microcos paniculata leaf, 20-22 pts. wt. amino acid, 15-17 pts. wt. humic acid and 200-220 pts. wt. water.    USE - Fertilizer composition used for cultivating Bauhinia (claimed).    ADVANTAGE - The fertilizer composition is prepared in eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a composition, which involves:    (A) mixing crushed raw materials with water, and then stirring them for 6-8 hours; and    (B) granulating the obtained material to obtain the finished product.
NOVELTY - Biofuel production involves performing microalgae cultivation by using cane sugar stillage (ethanol) through flocculation, separation, and drying disruption of cells. The formed biomass is fully extracted to obtain biofuel.    USE - Method for producing biofuel for use in diesel engines and turbines.    ADVANTAGE - They method produces biofuel with appropriate viscosity that reduces competitiveness to other fuels and energy consumption by motor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a photobioreactor column type. (Drawing includes non-English language text).
NOVELTY - Method for preparing formulation involves selecting and washing earthworm, soaking washed earthworm in water, where the weight ratio of washed earthworm and water is 1:10, and stirring, precipitating, and filtering soaked mixture.    USE - The method is useful for preparing formulation which is used for improving yield of okra (claimed).    ADVANTAGE - The method enables to prepare product in a cost-effective and environmentally-friendly manner, and which is rich in nutrients, and simple to prepare.
NOVELTY - Fertilizer comprises 120-140 parts mass horse dung, 30-40 parts mass dried orange peel, 20-40 parts mass Ageratina adenophora, 11-15 parts mass lees, 50-70 parts mass coal gangue, 8-12 parts mass molasses, 7-9 parts mass zeolite powder, 30-50 parts mass banana peel, 5-7 parts mass culture powder of bacteria, 30-40 parts mass wormwood, 20-30 parts mass willow, and 168-188 parts mass water.    USE - As fertilizer for Plumeria rubra (claimed).    ADVANTAGE - The fertilizer is rich in nutrients, improves soil texture, and can be easily absorbed by plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding the above-mentioned materials into crusher, adding water, crushing the materials, sealing and fermenting crushed product for 7-9 days, adding fermentation product to granulator, and collecting granules.
NOVELTY - Method for processing pig manure involves collecting pig manure and covering with layer of sawdust, inoculating Bacillus stearothermophilus, B.subtilis, actinomycetes, and Bifidobacterium, performing fermentation at 40-55 degrees C for 20-30 days, cooling fermented product, adding 0.5 wt.% supplement to cooled product, and performing fermentation at 15-30 degrees C for 30-60 days.    USE - The method is useful for processing pig manure (claimed).    ADVANTAGE - The method enables to process pig manure in a simple and environmentally-friendly manner.    DETAILED DESCRIPTION - Method for processing pig manure involves collecting pig manure and covering with layer of sawdust, inoculating 30-40 wt.% Bacillus stearothermophilus, 30-35 wt.% B.subtilis, 10-30 wt.% actinomycetes, and 10-15 wt.% Bifidobacterium, performing fermentation at 40-55 degrees C for 20-30 days, cooling fermented product to room temperature, adding 0.5 wt.% supplement to cooled product, where the supplement comprises 30-50 wt.% glucose powder, 20-30 wt.% lactic acid bacteria, 10-20 wt.% B.licheniformis, 10-20 wt.% Nitrobacter, and 5-10 wt.% nitrifying bacteria and performing fermentation at 15-30 degrees C for 30-60 days.
NOVELTY - Method for preparing plant cultivation material, involves (a) using 25-55 pts. wt. rice bran, 25-40 pts. wt. corn meal, 10-20 pts. wt. corncob, 5-18 pts. wt. oatmeal, 3-10 pts. wt. cottonseed hull and 1-8 pts. wt. sawdust, and (b) stirring and mixing the above-mentioned materials, and piling and fermenting mixture for one year.    USE - The method for preparing plant cultivation material used for indoor planting.    ADVANTAGE - The method is environmentally-friendly, causes no pollution, and prepares cultivation material having no peculiar smell. The cultivation material is organic and light weight, has high quality, loose structure and good ventilation effect and drainage performance, is rich in nutrients, and contains 84.2% organic substance.
NOVELTY - Preparing organic fertilizer involves (a) mixing chicken manure, fungal biomass waste, and enzyme mixture, and adjusting pH value of mixture, (b) heating the mixture, and fermenting heated mixture, (c) fermenting mixture by piling, and turning pile until hyphae develops, (d) screening fermented materials using a screening machine, and (e) passing the screened material into a granulator.    USE - The method is useful for preparing organic fertilizer (claimed), which is useful for improving disease resistance ability of plants, and antagonizing harmful bacteria.    ADVANTAGE - The method prepares fertilizer that enhances organic nitrogen, organic phosphorus, and organic potassium content in soil by not less than 3 times and soil oxygen by 5 times. The fertilizer increases soil fertility, changes pH of the soil, and prevents root rot in plants.    DETAILED DESCRIPTION - Preparing organic fertilizer involves (a) taking 800 kg chicken manure, 1200 kg fungal biomass waste, and 1 kg enzyme mixture, mixing the components, and adjusting pH value of the mixture to 6-8, (b) heating the mixture at 95-110 degrees C while stirring the mixture under atmospheric pressure, and fermenting the heated mixture for 7-9 hours, (c) fermenting the mixture by piling the mixture, maintaining temperature of the stack at 70-80 degrees C, and turning the pile 3-7 times once in every 3-4 days until hyphae develops, where the pile is of height of 2-3 m, (d) screening the fermented materials using a screening machine having screen size of not less than 0.5 cm, and (e) passing the screened material into a granulator.
NOVELTY - Organic fertilizer preparation involves taking 100-200 pts. wt. waste sisal hemp residue, 1-6 pts. wt. fermentation strain, 10-20 pts. wt. filtered mud, 1-4 pts. wt. urea, 1-2 pts. wt. ferrous sulfate, 1-2 pts. wt. zinc sulfate, 10-30 pts. wt. potassium dihydrogen phosphate and 10-20 pts. wt. alcohol waste liquid, and then mixing them except alcohol. The obtained material is fermented at 50-60 degrees C for 8-20 days to obtain fermented feed, and then the obtained fermented feed is dried. The obtained material is crushed, and then mixed them with alcohol waste liquid.    USE - Method for preparing organic fertilizer by using sisal hem waste residue (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer , which ensures improved soil property and yield of plant.    DETAILED DESCRIPTION - Organic fertilizer preparation involves taking 100-200 pts. wt. waste sisal hemp residue, 1-6 pts. wt. fermentation strain, 10-20 pts. wt. filtered mud, 1-4 pts. wt. urea, 1-2 pts. wt. ferrous sulfate, 1-2 pts. wt. zinc sulfate, 10-30 pts. wt. potassium dihydrogen phosphate and 10-20 pts. wt. alcohol waste liquid, and then mixing them except alcohol. The obtained material is fermented at 50-60 degrees C for 8-20 days to obtain fermented feed, and then the obtained fermented feed is dried. The obtained material is crushed, and then mixed them with alcohol waste liquid. The obtained material is granulated, and then packed them to obtain the finished product.
NOVELTY - Soilless cultivation matrix comprises organic cultivation matrix, inorganic fertilizer and 13.3-66.7 g water-retaining agent, where organic cultivation matrix comprises 50-75 pts. vol. fermented cassava residue, 0-50 pts. vol. peat and 0-35 pts. vol. vermiculite. The inorganic fertilizer comprises 0.33-1.67 kg urea, 0.07-0.39 kg inorganic phosphate and 0.22-1.12 kg potash mineral.    USE - Soilless cultivation matrix used for planting cucumber (claimed).    ADVANTAGE - The soilless cultivation matrix is prepared in eco-friendly manner, and ensures reduced loss of nitrogen from fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a soilless cultivation matrix, which involves:    (A) mixing fermented cassava residue, peat and vermiculite to obtain organic cultivation matrix;    (B) dissolving urea in water, and then adding water-retaining agent to the obtained material; and    (C) mixing the obtained material, and then adding inorganic fertilizer to obtain the finished product.
NOVELTY - P-nitrobenzoic acid, diethylaminoethanol and xylene are esterified, to obtain 4-Amino-benzoic acid 2-diethylamino-ethyl ester. Dilute hydrochloric acid is added to 2-diethylamino-2-amino-ethyl-4-nitrobenzoate, reacted and stirred, to obtain 2-diethylamino-2-amino-ethyl-4-nitrobenzoate hydrochloride. 2-Diethylamino-2-amino-ethyl-4-nitrobenzoate hydrochloride is hydrogenated, to obtain 2-diethylaminoethyl-4-aminobenzoate hydrochloride (2-diethylaminoethyl-4-aminobenzoate hydrochloride).    USE - Synthesis of procaine hydrochloride (claimed).    ADVANTAGE - The method enables environmentally-friendly synthesis of procaine hydrochloride with high yield, by simple method.
NOVELTY - Method for using earthworm for improving salinity of land, involves (a) selecting earthworm variety from multiple varieties of earthworm based on different pollution level and soil conditions, (b) collecting livestock manure and straw, and fermenting the livestock manure and straw, (c) processing soil including topsoil, (d) adding 120-200 kg earthworm to the processed soil per mu of land, (e) feeding the earthworm with fermented product, and (f) breeding earthworm and transferring newborn earthworm directly to the soil for improving salinity.    USE - The method is useful for improving salinity of land using earthworm (claimed).    ADVANTAGE - The method provides nutritional components required for plant growth, is cost-effective to perform, improves soil, and enables ecological breeding of earthworm.
NOVELTY - Method for processing toxic and hazardous organic pollutant-containing wastewater involves activating diluted wastewater in culture medium containing nitrogen and phosphorus sources, preserving the wastewater in culture medium to produce bacteria, changing the concentration of wastewater for every 2 days, packing a biofiller tower with mixture of magnetic filler, micro-electrolysis filler and filler carrier, introducing the wastewater into biofiller-packed tower, treating wastewater using bacteria to form biofilm, and carrying out electromagnetic-synergistic process.    USE - Processing of toxic and hazardous organic pollutant-containing wastewater (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables processing of toxic and hazardous organic pollutant-containing wastewater with excellent degradability and purifying characteristics.    DETAILED DESCRIPTION - Method for processing toxic and hazardous organic pollutant-containing wastewater involves diluting wastewater using distilled water, activating the diluted wastewater in culture medium containing nitrogen and phosphorus sources, preserving the wastewater in the culture medium to produce bacteria, changing the concentration of wastewater for every 2 days, packing a biofiller tower with mixture of magnetic filler, micro-electrolysis filler and filler carrier in mass ratio of 0.1-1.5:1-3:1-3, introducing the wastewater into the biofiller tower at 20-50 degrees C, treating the wastewater using the bacteria such that a biofilm is formed, and carrying out electromagnetic-synergistic process of wastewater by applying current density of 1-40 mA/cm2 and applied voltage of 0.1-5 V at 20-50 degrees C. The volume ratio of wastewater and distilled water is 1:100.
NOVELTY - Polymerization inhibitor comprises, primary amine (I), secondary amine (II), tertiary amine (III), diamine (IV) and polyamine (V).    USE - The polymerization inhibitor is useful for preventing self-polymerization of caprolactone (claimed).    ADVANTAGE - The polymerization inhibitor: can be used in small amounts for preventing self-polymerization in a simple, easy and environmental friendly manner; and reduces production costs of caprolactone.    DETAILED DESCRIPTION - Polymerization inhibitor comprises, primary amine of formula (R1-NH2) (I), secondary amine of formula (R2-NH2) (II), tertiary amine of formula (R4-N(R5)-R6) (III), diamine of formula (H2N-R7-NH2) (IV) and polyamine of formula (H2N-H2CH2C-(HNH2CH2C)n-NH-(CH2CH2NH)m-CH2CH2NH2) (V).    R1-R6 = 1-10C alkyl, 3-8C cycloalkyl, propenyl, benzyl derivative of formula (A) or phenyl derivative of formula (B1);    R7 = substituted phenyl derivative of formula (A1), substituted biphenyl derivative of formula (B2) or -CxH2x-;    R8, R9 = 1-5C alkyl, 1-5C alkoxy or H; either    n, m = 0-8; or    n+m = 0-8; and    x = 1-10.    An INDEPENDENT CLAIM is also included for the use method of polymerization inhibitor to prevent self-polymerization of caprolactone comprising, mixing polymerization inhibitor to caprolactone or caprolactone-containing material at 0-200 degrees C temperature with stirring and sealing, the amount of polymerization inhibitor is 0.0001-0.5 wt% of the entire material.
NOVELTY - High yield precocity wild rice plantation involves cutting head of seedlings after picking from 20 cm of bottom, and then providing 50 kg organic fertilizer per acre or 1000 kg manure for giving nutrients for the seedlings. The developed wild rice seedlings are transplanted to paddy fields in 3-5 cm depth at spacing control of 20x 20 cm, and then transplanted in a field at 3-5 cm depth at spacing control of 45x 70 cm in January. 50 kg organic fertilizer per acre or 1000 kg per acre manure is provided in the filed.    USE - Method for planting high yield precocity wild rice (claimed).    DETAILED DESCRIPTION - High yield precocity wild rice plantation involves cutting head of seedlings after picking from 20 cm of bottom, and providing 50 kg organic fertilizer per acre or 1000 kg manure for giving nutrients for the seedlings. The developed wild rice seedlings are transplanted to paddy fields in 3-5 cm depth at spacing control of 20x 20 cm, and then transplanted in a field at 3-5 cm depth at spacing control of 45asterisk70 cm in January. 50 kg organic fertilizer per acre or 1000 kg per acre manure is provided in the filed, and then 80-500 ml ethylicin is sprayed as fungicides per acre. The ripe crop is harvested.
NOVELTY - A microorganisms A592-4B (NITE P-01668), is new.    USE - The microorganism is useful as anionic substance adsorbent which is used for processing wastewater and in water purification method (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) water purification method involves contacting microorganism having adsorption capacity with respect to an water containing an anionic substance, where the microorganism belongs to genus Penicillium, adsorbing microorganisms with anionic substance in water and removing anionic substance; (2) method for processing wastewater involves processing wastewater containing an anionic substance by water purification method; and (3) anionic substance adsorbent comprising the microorganism.
NOVELTY - Hydrogen water refrigerating showcase comprises a clean water unit (100) for sending water purified by filtering with a first filter and a second filter to an electrolysis tank (210), an electrolytic unit (200) provided with a hydrogen storage filter (220) for storing hydrogen and the electrolysis tank for generating hydrogen by electrolyzing water purified from the clean water unit through diaphragm-free method, and an ultrasonic wave oscillating unit (300) for erupting hydrogen water dissolved hydrogen generated by the electrolytic unit in the form of spray through ultrasonic vibration.    USE - Used as hydrogen water refrigerating showcase.    ADVANTAGE - The showcase does not proliferate any microbes, maintains freshness and order of magnitude of water, has extended service life, sprays hydrogen water on the agricultural products, is harmless, and improves penetration and moisturizing effect while contacting with agricultural products.    DETAILED DESCRIPTION - Hydrogen water refrigerating showcase comprises a clean water unit (100) for sending water purified by filtering with a cylindrical first filter covered with activated charcoal and a second filter though reverse osmosis method to an electrolysis tank (210), an electrolytic unit (200) provided with a hydrogen storage filter (220) for storing generated hydrogen and the electrolysis tank for generating hydrogen by electrolyzing water purified from the clean water unit through diaphragm-free method, and an ultrasonic wave oscillating unit (300) for erupting hydrogen water dissolved hydrogen generated by the electrolytic unit in the form of spray through ultrasonic vibration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydrogen water refrigerating showcase (Drawing includes non-English language text).    Clean water unit (100)    Electrolytic unit (200)    Electrolysis tank (210)    Hydrogen storage filter (220)    Ultrasonic wave oscillating unit (300)
NOVELTY - This utility model claims a solar collection hot gas heating gas supply circulation system for farms in cold area, wherein a water pipe and one part farm heating system are connected, a part of the marsh gas tank, has one-way valve mounted in the air inlet, a mounting has shunt valve, a one-way valve, a pressure flow sensor, decompression valve, an air storage tank outlet and a marsh gas furnace and living with pneuma pipe connected at the outlet, a marsh gas furnace of heating pipe and one part farm heating system connection, a part of the marsh gas tank. This utility model solar collecting device is a water supply pipe in fermentation tank periphery means of gas storage marsh gas is used for extreme weather at a solar energy collecting heat heating auxiliary heat or for continuous and a marsh gas pool temperature supplement gas, solar energy heat collecting device a for farmers, provide human, livestock and domestic hot water, a water supply system of a gas furnace and solar energy collecting heat device, forming continuous supply heat for a pneuma, increase the heat can use.
NOVELTY - A dry shampoo composition comprises base and propellant. The base comprises sebum absorber comprises hollow particles.    USE - Dry shampoo composition is used for washing hair.    ADVANTAGE - The dry shampoo composition enables washing of hair without using water, and provides clean feel and good look.
NOVELTY - The device (10) has a seal unit that is located outwardly of the cathode chamber and placed between the electrolyte membrane and the cathode separator. The protective sheet unit includes a frame portion that faces the seal unit as a seal receiving portion in a stacking direction. A through hole formation portion is provided inwardly of frame portion. The through holes are formed in the through hole formation portion and provided from an inner to outer side in a range that faces the anode catalyst portion in the stacking direction.    USE - High pressure water electrolysis device for producing hydrogen gas used as fuel gas for power generation reaction in fuel cell.    ADVANTAGE - The damage of the electrolyte membrane is prevented as much as possible with a simple configuration, and improvement in water supply performance and gas release performance are achieved. The depressurization time of the high pressure water electrolysis device is reduced and the operation efficiency is favorably improved. The blister does not occur in the electrolyte membrane, and high pressure hydrogen dissolved in the electrolyte membrane is easily and reliably discharged at the time of depressurization with a simple configuration, and the durability of the electrolyte membrane is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective of a high pressure water electrolysis device.    High pressure water electrolysis device (10)    Unit cell (12)    Layer housing (14)    Tie rod (22)    Electrolytic power supply (28)
NOVELTY - Aniline compound or its salt is prepared which involves hydrogenation of 2'-benzyloxy-3'-nitrobiphenyl-3-carboxylic acid or its salt; and optionally, conversion of aniline compound to its salt, or vice versa.    USE - The processes are useful for preparing aniline compound of formula (II) or its salt, and 2'-benzyloxy-3'-nitrobiphenyl-3-carboxylic acid of formula (III) or its salt (claimed) used for preparing Eltrombopag for treating patients suffering from immune thrombocytopenic purpura (ITP).    ADVANTAGE - Alternative, improved preparation method is provided for aniline compound of formula (II) consequently Eltrombopag of formula (I), which is simpler and more advantageous. It comprises a smaller number of synthesis steps. The intermediates can be synthesized and purified more easily on an industrial scale. The process is also cheap, and safe for humans and the environment. It uses mild reaction conditions to obtain Eltrombopag of formula (I) with high yields and efficiency.    DETAILED DESCRIPTION - Aniline compound of formula (II) or its salt is prepared which involves hydrogenation of 2'-benzyloxy-3'-nitrobiphenyl-3-carboxylic acid of formula (III) or its salt; and optionally, conversion of aniline compound of formula (II) to its salt, or vice versa.    R and R'=the same or different, independently hydrogen, a 1-6C alkyl group, or an aryl group; and    Ar'=an aryl group.    INDEPENDENT CLAIMS are included for:    (1) a compound selected from 2'-benzyloxy-3'-nitrobiphenyl-3-carboxylic acid of formula (III) or its salt, in particular in crystalline form; and benzyl 2-bromo-6-nitrophenyl ether of formula (IV) or its salt, in particular in crystalline form; and    (2) a process for preparing 2'-benzyloxy-3'-nitrobiphenyl-3-carboxylic acid of formula (III) or its salt which involves reacting benzyl 2-bromo-6-nitrophenyl ether of formula (IV) with boronic acid of formula (V), or its salt, in Suzuki conditions.    Y'=a leaving group.
NOVELTY - Method (M1) of processing waste stream involves (a) transporting heterogeneous waste stream comprising biodegradable waste and non-biodegradable waste to waste processing system, (b) receiving the heterogeneous waste stream, (c) delivering food products to food retailing facility, (d) separating the biodegradable waste from the non-biodegradable waste, and (e) digesting the biodegradable waste anaerobically in an anaerobic digester in the waste processing system to produce biogas.    USE - The method involves processing waste stream which is used for producing biogas and fertilizer (all claimed).    DETAILED DESCRIPTION - Method (M1) of processing waste stream involves (a) transporting heterogeneous waste stream comprising biodegradable waste and non-biodegradable waste from food retailing facility to waste processing system located remotely from the food retailing facility utilizing a shared transportation infrastructure, (b) receiving the heterogeneous waste stream at the waste processing system, (c) delivering food products from food distribution facility co-located with waste processing facility to the food retailing facility utilizing the shared transportation infrastructure, (d) separating the biodegradable waste from the non-biodegradable waste, and (e) digesting the biodegradable waste anaerobically in an anaerobic digester in the waste processing system to produce biogas. An INDEPENDENT CLAIM is included for method (M2) of waste recovery, conversion, and utilization involves (a) receiving food products from food supplier at a food product distribution facility, (b) delivering the food products to several food retailers, (c) delivering a heterogeneous waste to the food product distribution facility, and (d) producing a biogas from the heterogeneous waste in an anaerobic digester in a waste processing facility co-located with the food product distribution facility.
NOVELTY - Use of extracellular polymeric substances obtained from granular sludge for sizing paper and paper-like product, is claimed.    USE - Use of extracellular polymeric substances obtained from granular sludge in sizing of paper and paper-like product (all claimed).    ADVANTAGE - The method provides paper having excellent water resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sizing of paper.
NOVELTY - Manufacture of biodiesel from plant oil involves using methyl acetate as reagent and sodium methoxide solution of methanol as catalyst. The biodiesel is manufactured in one stage with simultaneous glycerol conversion into its derivatives.    USE - Manufacture of biodiesel used as fuel for diesel engine and heating device.    ADVANTAGE - The method provides biodiesel with high quality at low temperature and atmospheric pressure in a short period of time.
NOVELTY - The system (10) has a low pressure gas-liquid separator (52) that is placed in a drain line (46) and having a discharge line (60) through which a gas separated by the low pressure gas-liquid separator is to be discharged. A water return line (56) connects the low pressure gas-liquid separator and the water supply tank (28). A pressure maintaining mechanism is placed in discharge line and configured to maintain a pressure in low pressure gas-liquid separator to be higher than a pressure in the water supply tank.    USE - High differential pressure water electrolysis system for generation of hydrogen used as fuel gas for power generation reaction in fuel cell.    ADVANTAGE - The water in the low pressure gas-liquid separator is easily and reliably returned to the water supply tank due to a pressure difference. Thus, the utilization of dedicated equipment and the pressure of the dissolved hydrogen are not needed. The efficiency of the entire high differential pressure water electrolysis system is improved, and miniaturization of the high differential pressure water electrolysis system is achieved. The reuse of water is achieved easily and cost-effectively, in order to achieve improvement in the system efficiency and miniaturization of the entire system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for starting high differential pressure water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a high differential pressure water electrolysis system.    High differential pressure water electrolysis system (10)    Water supply tank (28)    Drain line (46)    Low pressure gas-liquid separator (52)    Water return line (56)    Discharge line (60)
NOVELTY - An energy-saving metal alcohol oil fuel composition comprises 50-90 wt.% methanol, 10-30 wt.% water, 0.01-0.08 wt.% ferrocene, and 0.1-20 wt.% emulsifier.    USE - Energy-saving metal alcohol oil fuel composition.    ADVANTAGE - The method has wide source of raw materials and low cost and is simple and easy quality control. The composition has high heat value, stable, colorless, tasteless, no smoke, and no explosion combustion, and more than 200 degrees C ignition temperature, and greatly increases safety performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fuel composition comprising mixing emulsifier raw materials and fully stirring; and adding methanol to reaction kettle, adding water and emulsifier, and fully stirring for 20-30 minutes.
NOVELTY - Thermodissociating hydrogen and oxygen generator contains a steam generator, a rotating steam collector with holes for steam release, plasmochemical reactors for thermal dissociation of water vapour and obtaining of hydrogen and oxygen which are connected to the power supply and which are interconnected from one side with holes in the steam collector and from another side - with expanding nozzles and cylinders of wave compressors. The plasmochemical reactors either consist of a housing in which a cathode electrode is installed and which has a jacket interconnected with a cooled anode nozzle, and the front surface of the housing is implemented as a disk with holes for steam supply, or plasmochemical reactors are implemented as a block of reactor housings which are interconnected with the block of cooled anode nozzles, the housings contain cathode electrodes, on the block of plasmochemical reactors the valve mechanism for steam intake is located. Plasmochemical reactors, expanding nozzles and cylinders of wave compressors have jackets for cooling liquid circulation.    USE - Power industry.    ADVANTAGE - Decrease of cost of finished goods.6 dwg
NOVELTY - The pool has a fermentation pool body provided with a rectangular-shaped shell. An inner part of the rectangular-shaped shell is formed with a rectangular fermentation groove. A bottom part of the fermentation groove is matched with an electric agitator blade. A top part of the rectangular fermentation groove is matched with a two-level feeding port. A feeding and discharging unit is matched with the bottom part of the rectangular fermentation groove. A top part of a liquid seal transfer groove is formed with a reflux liquid inlet. A secondary feeding port is matched with a rotary seal cover.    USE - Sludge treatment Anaerobic fermentation pool.    ADVANTAGE - The pool ensures that a seal system is formed with a normal fermentation groove by the reflux liquid inlet so as to improve normal fermentation groove sealing effect, thus realizing electric stirring paddle stirring process and improving Anaerobic fermentation product quality, and hence passing heat to the reflux liquid inlet. The pool increases fermentation temperature of the normal fermentation groove so as to improve working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a sludge treatment anaerobic fermentation pool.
NOVELTY - Removal of low boiling components from crude methyl ester involves transferring crude methyl ester to flash tank, heat-exchanging, vacuum distilling low-boiling components, analyzing, separating, pulling low boiling components with vacuum pump, removing low boiling components of crude methyl ester from bottom of the flash tank, mixing biodiesel at high temperature and crude methyl ester feedstock in a mixer, collecting biodiesel, heating crude methyl ester, and removing low-boiling components.    USE - Removal of low boiling components from crude methyl ester (claimed).    ADVANTAGE - The method enables simple removal of low boiling components from crude methyl ester, and improves product purity and quality.    DETAILED DESCRIPTION - Removal of low boiling components from crude methyl ester involves transferring crude methyl ester to flash tank using negative pressure method, heat-exchanging, vacuum distilling low-boiling components, analyzing, separating, pulling low boiling components with vacuum pump, removing low boiling components of crude methyl ester from bottom of the flash tank, mixing biodiesel at high temperature and crude methyl ester feedstock in a mixer, such that the temperature of the crude methyl ester increases and temperature of the biodiesel decreases, collecting biodiesel, heating crude methyl ester, and removing low-boiling components. The low boiling crude methyl ester is biodiesel.
NOVELTY - The heating device (900a) has tube main portion whose ends are provided with liquid inlet and liquid outlet. The heating cavity is provided with the liquid inlet and liquid outlet. The inner side wall of main portion is provided with mounting surfaces. A power supply mechanism (940a) is respectively connected with heating pipes (920a,930a) for providing power to the heating pipes.    USE - Heating device.    ADVANTAGE - The heating operation is carried out for pre-processing domestic garbage, so that good anaerobic fermentation effect is obtained. The heating device is environment-friendly. The energy saving efficiency of the device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the heating device.    Heating device (900a)    Discharge port (912b)    Heating pipes (920a,930a)    Power supply mechanism (940a)
NOVELTY - Apparatus comprises an animal manure processing unit (6) that is inclined toward the center position of the funnel-shaped container. The apparatus also comprises a wastewater processing unit (7) and a wastewater separation unit (9) for processing waste oil spills in the form of foam, which are then separated. The solid impurities are removed using a filter assembly (11). Mixing unit (12) is provided for mixing animal manure and waste water in certain ratio, and then obtained material is fed into a tank (15).    USE - Apparatus used for processing farm waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing farm waste, which involves:    (A) processing farm waste into the purification unit, and then subjecting into a mixing unit comprising formulated animal manure and wastewater to obtain a feedstock mixture; and    (B) performing fermentation at controlled at 35 degrees C, where the feedstock mixture recycling are digested to produce biogas and bagasse, where the rate of biogas production is adjusted by the control unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a farm waste processing apparatus.    Animal manure processing unit (6)    Wastewater processing unit (7)    Wastewater separation unit (9)    Filter assembly (11)    Mixing unit (12)    Tank (15)
NOVELTY - Crystalline levopraziquantel (I) exhibiting X-ray powder diffraction pattern using (copper-potassium alpha radiation) at 25 degrees C with peaks as given in the specification are, new.    USE - (I) are useful for preventing and/or treating parasitic diseases (claimed).    ADVANTAGE - (I): have good solubility, drug effect and pharmacokinetics. The method: has good repeatability; is environmentally friendly and economical; can be performed at normal pressure and temperature; and is suitable for large-scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of (I); and #composition useful for preventing and/or treating parasitic diseases, comprising (I) and a carrier.
NOVELTY - Producing green coffee bean extract comprises taking green coffee beans, subjecting for carbon dioxide supercritical process, then using organic solvent for extracting to obtain the product.    USE - The method is useful for producing green coffee bean extract (claimed).    ADVANTAGE - The method has simple operation, ensures the retention of active component (chlorogenic acid) content, can save energy consumption, uses carbon dioxide supercritical technology to replace normal hexane and methylene dichloride to remove lipid series substance and caffeine, can greatly reduces pesticidal rudimental, obtains the product with yield of more than 11%, increases the filtering efficiency, reduces production cost, does not produce harmful solvent residue, is economical, and is suitable for large-scale industrial production, and has great application prospect and economic value. The green coffee bean extract has antioxidant, antiviral, and anticancer properties; and has good fluidity and high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for green coffee bean extract comprising 28-37 wt.% 5-caffeoylquinic acid, 2-7 wt.% 3-caffeoylquinic acid, 2-6 wt.% 4 caffeoyl quininic acid, 0.2-4 wt.% 3,4-dicaffeoylquinic acid, 0.2-4 wt.% 3,5-dicaffeoylquinic acid, 0.15-2 wt.% 4,5-dicaffeoylquinic acid, preferably 5-caffeoylquinic acid is 34-37 wt.%.
NOVELTY - (1R,2R)-Cyclohexane-1,2-diyldimethanol is mesylated, to obtain (1R,2R)-1,2-bis(methanesulfonyloxymethyl)cyclohexane. The obtained product is reacted with 3-(piperazin-1-yl)benz(d)isothiazole in an organic solvent in the presence of a calcium or magnesium oxide or hydroxide, to obtain (3aR,7aR)-4'-(benz(d)isothiazol-3-il)octahydrospiro(2H-isoindol-2,1'-piperazinium)methanesulfonate. The obtained product is reacted with (3aR,4S,7R,7aS)hexahydro-1H-4,7-methanoisoindole-1,3(2H)-dione, to obtain lurasidone.    USE - Preparation of lurasidone useful as a typical antipsychotic drug which is useful in treatment of schizophrenia, bipolar disorder and other psychiatric conditions.    ADVANTAGE - The method enables environmentally-friendly preparation of lurasidone with high yield and purity of more than 99% measured by HPLC, using cheap reagents of low toxicity by simple and quick process.
NOVELTY - Cultivating organic selenium involves keeping the plant in an incubator (3) with an aqueous solution of selenium and then entering the incubated material into feeding device (7), breeding tank (1) and sliding parking rail (2) through ultrasonic wave generator (4). The obtained material is cultured, heated, atomized, subjected for sewage treatment, treated with clean water, dried and packaged, where the whole process is controlled and monitored automatically.    USE - Method for cultivating organic selenium used in biological processes (claimed).    ADVANTAGE - The method enables to cultivate organic selenium in safe and non toxic manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram for a method for cultivating organic selenium.    Breeding tank (1)    Sliding parking rail (2)    Incubator (3)    Ultrasonic wave generator (4)    Feeding device (7)
NOVELTY - This new type utility claims the domestic garbage machine biological leaching filter processing comprehensive use system, wherein the discharge feed and wherein aerobic biological filter l shower comprises a pre-processing unit, an aerobic biological filter l shower, pool and aerobic bioreactor, pre-process unit is connected, wherein the liquid inlet outlet and wherein the digestion pool is aerobic biological leaching filter l is connected, a pool wherein the liquid outlet and liquid inlet wherein the aerobic bioreactor is connected, the air inlet of the aerobic bioreactor through circulation fan and aerobic biological leaching filter l is connected air outlet, further comprising filter shower nozzle and shower filter pump, a shower nozzle set in the aerobic biological filter shower filter l inner, filter head shower through filter pump and aerobic bioreactor connected, further comprising dewatering machine. This utility new type using a structure, it can make the domestic garbage is decomposed completely, each effective component in the garbage is fully use, for a comprehensive use of domestic garbage, and gas and liquid to a. there is no pollute, for it has good environment protection effect.
NOVELTY - Phase two. This utility new type relates to a organic waste water hydrolysis acidification coupling a culture of microalgae, belongs to biological engineering field. This system comprises distribution water tank waste water, organic waste water biological hydrolysis acidification pre-processing reaction phase, micro-algae mixed health preserving long light biological culture. phase and the middle connecting device, wherein waste water distribution water tank storing organic waste water, the waste water from the waste water with water tank through pipeline pump into the organic waste water biological hydrolysis acidification pre-processing reaction the inner, biological hydrolysis acidification pre-processing reaction through pipeline and the middle is connected with a connected, hydrolysis acidification pre-processing biological reaction is provided with convenient for disassembling a liquid filter cartridge device and the middle connected device; the middle connecting device and organic waste water biological hydrolysis acidification pre-processing reaction phase exit. micro-algae mixed health preserving long light biological culture. tank body which a has a liquid inlet hole and the middle is connected a. this system a finish effective reduce the waste water COD, and obtaining microalgae oil of high biological quantity, a organic waste water is clean.
NOVELTY - This utility new type relates to a discharge, a collection system, specifically claims a green energy-saving building a discharge collection processing system, solving the technology problem is supply the planting a fully enclosed, energy-saving and environment-friendly, natural, health and comfortable is green energy-saving building exhaust collection processing system, using the technology scheme is a sewage inlet of the coarse fine grate and sand-precipitating device and regulating pool connected, the regulating pool is outlet and Anaerobic fermentation tank is connected with the inlet, a drain and wherein biogas pool.. Anaerobic fermentation tank are connected, liquid biogas residue pool. has a green cast-pour pump. Anaerobic fermentation tank of a methane gas outlet positive and negative pressure protector and pneuma water separator is connected, the pneuma water separator, a flame arrester and a table is connected, this utility new type is widely used for a dirt discharge and collection.
NOVELTY - An organic material decomposing agent comprises Lactobacillus delbrueckii, Bacillus licheniformis and Aspergillus niger at mass ratio of 5-20:10-70:1-10, where mixed concentration is not less than 50 hundred million/g of composite.    USE - Organic material decomposing agent.    ADVANTAGE - The decomposing agent has high humic acid content and has 95% germination percentage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process of organic material decomposing agent fermentation comprising regulating organic raw material total water of 50-65%, total nutrient content of 6% and total organic matter content of 55%, taking organic material decomposing agent, mixing, fermenting for 5-7 days at 60 degrees C, maintaining moisture content to 40%, crushing, and carrying out second fermentation for 20 days.
NOVELTY - A green tea special fertilizer comprises 50-60 pts. wt. chicken manure, 5-10 pts. wt. tea leaves, 5-10 pts. wt. tea tree, 5-10 pts. wt. straw powder, 5-10 pts. wt. cornmeal, 5-20 pts. wt. urea, 10-20 pts. wt. potassium tripolyphosphate, 10-20 pts. wt. sodium metaphosphate, 1-2 pts. wt. citric acid, 2-3 pts. wt. gypsum powder, 1-2 pts. wt. fermentation microbial inoculum, and balance water.    USE - Green tea special fertilizer.    ADVANTAGE - The fertilizer can increase yield and quality of tea and increase soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special fertilizer comprising collecting waste tea leaves and tea tree, adding chicken manure and water, stirring, adding remaining raw materials, piling to carry out composting, covering with plastic film, fermenting to 45 degrees C, and cooling.
NOVELTY - Preparation of floral composite nutrient soil comprises taking sewage treatment plant sludge and naturally airing; mixing sludge, sawdust, bone meal, peat, straw powder, potassium permanganate, ferrous sulfate and ceramic, crushing, and adding water to obtain material; and adding active microorganism per ton of material, stirring at room temperature, anaerobically fermenting, and turning.    USE - Method for preparing floral composite nutrient soil (claimed).    ADVANTAGE - The method has inexpensive sludge sources, reduces release rate of the fertilizer and cost of the nutrient soil, and increases utilization of plant nutrients.    DETAILED DESCRIPTION - Preparation of floral composite nutrient soil comprises taking sewage treatment plant sludge and naturally airing until moisture content of less than 70%; mixing 20-30 pts. wt. sludge, 15-20 pts. wt. sawdust, 10-20 pts. wt. bone meal, 20-30 pts. wt. peat, 8-10 pts. wt. straw powder, 0.005-0.01 pt. wt. potassium permanganate, 0.05-0.1 pt. wt. ferrous sulfate, 10-20 pts. wt. ceramic with particle size of less than 0.4 mm, crushing, and adding water to obtain material with moisture content of 70-80%; and adding 2-kg active microorganism per ton of material, stirring at room temperature, anaerobically fermenting for 12-24 hours, and turning for 30-40 days.
NOVELTY - Continuous synthesis of 1,3-diphenylguanidine comprises taking aniline and solvent, feeding into continuous flow pressure tube reactor, adding cyanogen chloride, reacting at 140-190 degrees C for 2-5 minutes, filtering, neutralizing, purifying and drying.    USE - Method for continuous synthesizing of 1,3-diphenylguanidine (claimed).    ADVANTAGE - The method has 96.5-98.9% yield and 99.42-99.71% purity.