NOVELTY - The utility model claims a fertilizer production device, specifically a strain culture tank for producing high efficient microbe bacteria fertilizer. A tank body, is provided with a feed inlet and the inoculating port at the upper end of the tank body is provided with a discharging port on the lower end of the tank body, the outer wall of the tank body is provided with an interlayer water sleeve, the upper end of the water jacket is provided with a medium outlet, the lower end of the water jacket is provided with a medium inlet, it is set with a rotating shaft in the tank body, the two ends of the rotating shaft is installed on the inner wall of the tank body through the bearing, the middle section of the rotating shaft is equipped with a shell, wherein the shell is a concave one surface bulge of the shell, a shell is fixedly connected to the rotating shaft, a plurality of spherical shell are uniformly distributed is set around the four sides of the rotating shaft. The culture tank to realize non power stirring, saves energy, namely material can be uniformly mixed, but also can prevent the culture medium surface to form hard shell, which is good for cultivating the strain.
NOVELTY - The utility model claims a biological bacterium fertilizer production device, specifically to a method for producing a fermentation tank for efficient biological bacteria fertilizer. A tank body is cylindrical, the upper end of the tank body is provided with a feeding port at the lower end is provided with a discharge port, a feed port and a discharge port are arranged on the side of the tank body, the bottom of the tank body is connected with a discharging pipe, the discharging pipe is equipped with a discharging valve, the top of the inner cavity of the tank body is provided with an air bag, an air inlet nozzle of the air bag is connected with the air pump. The fermentation tank through the air capable of adjusting internal volume and pressure, so as to adapt to different batch production of the ferment strain number, is in favour of reducing production equipment investment, improves the consistency of the product.
NOVELTY - This utility model claims a kind of organic waste aerobic biological treatment device, comprising a front panel, a back panel, a left panel, a right panel and a panel to form a cavity according to the plurality of panel is equipped with supporting frame and is set with the reaction mechanism on the supporting frame inwards on the cavity body, a reaction mechanism for holding organic waste and to carry out biochemical treatment for the reaction chamber, is provided with a water discharging part in the wall of the reaction chamber, the drainage part is provided with protruding towards the inner side of the reaction chamber surface part extending towards the inner side of the reaction chamber and is connected with the convex side part of the cylinder part is provided with a first drainage hole is connected with the reaction chamber of the upper part in the cylinder part of the side wall, it can avoid organic waste block a drainage hole, the drainage more smooth so as to ensure organic waste aerobic bio-treatment device smoothly.
NOVELTY - This utility model claims a kind of a fertilizer turning machine, comprising a machine frame, a driving chain wheel, a transmission shaft, a transmission chain wheel, a traction chain, a transmission chain, a driven chain wheel, a gear plate and a gear, the transmission shaft is embedded with a transmission chain wheel, a machine frame is provided with a driven chain wheel and a driving chain wheel, a driven chain wheel and the driving chain wheel are connected with each other through the traction chain, the middle part of the machine frame is provided with a transmission shaft, the transmission shaft and the upper part is embedded with a transmission chain wheel, a transmission chain wheel and the driving chain wheel are connected by a transmission chain, the lower side surface of the traction chain is provided with one end of the gear base plate, gear plate is provided with a rack. This utility model claims a kind of fertilizer turning machine frame, a transmission shaft, a transmission chain under the condition without changing the implementation of a traction chain tensioning, two driven chain wheel are set in parallel at intervals, the driven shaft to ;T the break gear to prevent leakage.
NOVELTY - The utility model claims a fertilizer production device, specifically to a microorganism bacterium fertilizer production device, comprising a shell and a shell body of the stirring shaft, the upper end of the stirring shaft extends to the outer side of the shell, is connected with the output shaft of the motor located on the outer side of the shell, wherein the shell is internally provided with the inner side plate is arc-shaped, the inner side plate can be set in the shell, because of adopting said structure, this utility model is the one kind of microorganism bacterium fertilizer production device of material on the inner side stress of ball mill lining plate is different, it will generate a key, so a more uniform, and the material at the edge can increase the contact probability with the stirring shaft for extruding, the stirring is more uniform.
NOVELTY - Method for preparing pharmaceutical composition, involves extracting Salvia miltiorrhiza using water or ethanol solution as extracting solvent, controlling pressure, heating extract, and refluxing product.    USE - The method is useful for preparing pharmaceutical composition (claimed).    ADVANTAGE - The method can improve content of effective component of S.miltiorrhiza and reduce high temperature heating time caused by long root, extraction time and solvent consumption.
NOVELTY - The utility model claims a fertilizer production device, specifically to a de-starch bacillus shaking culture box, comprising a box body, an oscillator unit in the box body and a motor located on the outer side of the box body, wherein the box body is further provided with a heating pipe, wherein the oscillator is connected with the box spring, oscillating in the oscillator is provided with a containing test tube shelf, said shelf comprises a plurality of parallel arranged with the object, because of adopting said structure, this utility model is the one kind of bacillus amyloliquefaciens shaking culture box can inserted the pipe diameter of the inserting hole for a test tube and taking is very convenient, and the test tube will not be fixed, which can be mixed for oscillation of the test tube, making air and fuel gas mix more uniform and complete reaction.
NOVELTY - Method for extracting andrographolide from Andrographis involves crushing Andrographis plant, adding water and ethanol solution to crushed plant, extracting with water, adding water and ethanol to extracting solution, adjusting pH, adding cellulase, performing enzymolysis, extracting using ultrasonic-microwave extraction device, centrifuging extraction liquid, adding petroleum ether, removing chlorophyll fat-soluble impurity, concentrating, preprocessing macroporous absorption resin, eluting using ethanol solution, decompressing, concentrating, and crystallizing.    USE - Method for extracting andrographolide from Andrographis plant.    ADVANTAGE - The environmentally-friendly andrographolide is manufactured efficiently and economically with high purity, high extraction rate and productivity.    DETAILED DESCRIPTION - Method for extracting andrographolide from Andrographis involves crushing Andrographis plant, adding water and ethanol solution to the crushed plant, extracting with water using extractor with rotating speed of 2000-4000 r/minute for 1-2 minutes, adding water and ethanol to extracting solution, adjusting pH to 4.5-5.5, adding 0.04-0.6 wt.% cellulase, performing enzymolysis at 45-55 degrees C for 2-3 hours, stirring, extracting using ultrasonic-microwave extraction device with ultrasonic wave power of 600 W and microwave power of 200-300 W, centrifuging extraction liquid, removing supernatant fluid, adding petroleum ether, removing chlorophyll fat-soluble impurity, concentrating, preprocessing macroporous absorption resin, eluting using ethanol solution, decompressing, concentrating, and crystallizing ethanol.
NOVELTY - Preparation of strawberry fertilizer, involves (a) slicing plant straw, covering bottom of container with a layer of gauze, covering with a uniform thickness, layering sand over the layer of straw, and maintaining temperature, (b) inoculating earthworm on straw, fermenting mixture at 20-25 degrees C for 50-55 days, and maintaining ambient humidity to 55-65%, and (c) adding nitrogen (N), phosphorus (P), and potassium (K) to the container, adding 20% substrate into the container, and mixing mixture to obtain fertilizer.    USE - The method is useful for preparation of strawberry fertilizer for reducing heavy metal pollution (claimed), preferably lead, mercury, chromium and other heavy metals.    ADVANTAGE - The method is environmentally-friendly, reduces usage amount of chemical fertilizer and reduces organic waste, thus saves planting cost.    DETAILED DESCRIPTION - Preparation of strawberry fertilizer, involves (a) slicing plant straw to 2-4 cm length, covering bottom of container with a layer of gauze, covering with a uniform thickness of 15-20 cm straw, layering 3-6 cm sand over the layer of straw, and maintaining temperature at 20-25 degrees C, (b) inoculating earthworm on straw, where stocking density of ??the container is 60-80 per m2, fermenting mixture at 20-25 degrees C for 50-55 days, and maintaining ambient humidity to 55-65%, and (c) adding nitrogen (N), phosphorus (P), and potassium (K) to the container, adding 20% substrate into the container, and mixing mixture to obtain fertilizer. An INDEPENDENT CLAIM is included for reducing heavy metal pollution by applying prepared fertilizer, which involves (a) breeding fertilizer 40-60kg/acre, seedling for 10-15 days, and producing 80-100 kg/acre fertilizer, (b) producing in growing season by applying the fertilizer to 200-300 kg/acre, and (c) applying 40-60 kg/acre farmyard manure, and processing the fertilizer by topdressing.
NOVELTY - Preparation of agricultural organic fertilizer comprises mixing chicken manure and straw, fermenting to obtain fermentation mixture, drying, and mixing with fly ash.    USE - Method for preparing agricultural organic fertilizer (claimed).    ADVANTAGE - The fertilizer has low cost and can improve yield of vegetables.
NOVELTY - An antisalt bacterial biofertilizer formulation comprises nutritional support, additive, trace element, and microorganism fermentation liquor. The fertilizer has viable bacteria level of greater than or equal to 101 colony forming unit (cfu)/ml, total nutrient of greater than or equal to 12%, solid particle size of 0.1 mm, and viable preservation content of 108 cfu/ml.    USE - Antisalt bacterial biofertilizer formulation used for drip irrigation for cotton, tomatoes, and wheat cultivation, mitigating soil salinization, preventing seedling soil-borne diseases, and promoting crop growth (claimed).    ADVANTAGE - The formulation has liquid dosage form, long shelf life, and bacteria effective viable count of not less than 1010 cfu/ml.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of formulation by dissolving nutritional support in water, mixing with additive and trace element, and sterilizing to 121 degrees C; and mixing with microorganism fermentation liquor.
NOVELTY - An oyster mushroom cultivation material comprises 20-30 wt.% chestnut tree meal, 18-22 wt.% corn meal, 12-18 wt.% oak chip, 20 wt.% cotton seed hull, 17 wt.% wheat bran, 1 wt.% gypsum powder, and 2 wt.% lime.    USE - Oyster mushroom cultivation material.    ADVANTAGE - The material has reasonable thickness, good air permeability, and vigorous mycelium growth of oyster mushroom. The method removes toxic antimicrobial material, allows degradation of macromolecules, promotes formation of fruiting body primordia, increases production of mushroom by 20-30%, and has reduced production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of material by mixing raw materials, exposing in sun for 1-2 days, and killing bacteria through UV light while simultaneously decomposing volatile antibacterial substances; (B) mixing chestnut tree meal, corn meal, and oak chip, and adding lime aqueous solution to obtain wet material; (C) piling with 300-500 kg dry material at 1-1.2 m high and 2-3 m wide, stacking with 10-15 cm stick in vertical air holes, covering with straw, and naturally fermenting; (D) turning pile once a day when temperature reaches 60 degrees C for 24 hours, adding cotton seed hull, wheat bran, corn flour, and gypsum powder in third turning, adding water depending on moisture content of material, turning for 4-5 times for 6-7 days, and stopping fermentation until moisture content is 63-65%; (E) bagging 1100-1200 g wet material in 17 cmx 35 cmx 0.005 cm polypropylene bags to carry out inoculation; and (F) sterilizing at 100 degrees C for 10-12 hours, and cooling to 25 degrees C or less.
NOVELTY - A mushroom cultivation material comprises 15-25 wt.% chestnut tree meal, 14-18 wt.% corn meal, 7-13 wt.% oak chip, 15 wt.% corn cob, 10 wt.% cottonseed hull, 18 wt.% wheat bran, 8 wt.% soybean meal, 1 wt.% gypsum powder, and 2 wt.% lime.    USE - Mushroom cultivation material.    ADVANTAGE - The method removes toxic antimicrobial material, allows degradation of macromolecules, promotes strong growth of mycelium, and has reduced production cost. The material has water-holding capacity, effective mushroom quantity, and biological efficiency of 107.5-115.2%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of material by mixing raw materials, exposing in sun for 1-2 days, and killing bacteria through UV light while simultaneously decomposing volatile antibacterial substances; (B) mixing chestnut tree meal, corn meal, and oak chip, and adding lime aqueous solution to obtain wet material; (C) piling with 300-500 kg dry material at 1-1.2 m high and 2-3 m wide, stacking with 10-15 cm stick in vertical air holes, covering with straw, and naturally fermenting; (D) turning pile once a day when temperature reaches 60 degrees C for 24 hours, adding corn cob, cotton seed hull, wheat bran, soybean meal, and gypsum powder in third turning, adding water depending on moisture content of material, turning for 4-5 times for 6-7 days, and stopping fermentation until moisture content is 63-65%; (E) loading in 1100 mlx 78 mmPP plastic bottles, making 16 mm holes, and covering with breathable foam caps to carry out inoculation; and (F) placing in autoclave, sterilizing at 100 degrees c for 1 hour, raising temperature to 121 degrees C for 1.5 hours, and cooling to below 25 degrees C.
NOVELTY - A mushroom culturing material comprises 20-30 wt.% chestnut branch chips, 16-20 wt.% bud shell chips, 9-15 wt.% chestnut shell chips, 20 wt.% corncob, 16 wt.% wheat bran, 6 wt.% soybean meal, 1 wt.% gypsum powder and 2 wt.% lime powder.    USE - Mushroom culturing material.    ADVANTAGE - The culturing material removes toxic bacteria and degrades macromolecular substances. It has reasonable proportion, good ventilation property and strong water-preserving property. It has biological efficiency of 107.4-115.6%, thus greatly reducing production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom culturing material comprising drying raw materials for 1-2 days, killing bacteria by UV light, pre-wetting chestnut branch chips, bud shell chips and chestnut shell chips by 2% aqueous lime solution, uniformly stirring, stacking, plugging air holes, covering upper part with tarpaulin, naturally fermenting, turning when temperature reaches 60 degrees C, keeping for 24 hours, adding corncob, wheat bran, soybean meal, gypsum powder and water, turning 4-5 times for 6-7 days, putting in polypropylene plastic bag, sterilizing at 100 degrees C for 10-12 hours and naturally cooling to lower than 25 degrees C.
NOVELTY - Hydrogen storage power supply system comprises a solar battery set (1), controller (2), balance energy storage unit (3), inverter (4), air generator (5), electrolytic hydrogen producing machine (7), curing hydrogen-storage unit (8) and hydrogen energy generator (9).    USE - Hydrogen storage power supply system for solar water pump.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the hydrogen storage power supply system.    Solar battery set (1)    Controller (2)    Balance energy storage unit (3)    Inverter (4)    Air generator (5)    Electrolytic hydrogen producing machine (7)    Curing hydrogen-storage unit (8)    Hydrogen energy generator (9)
NOVELTY - Manufacture of biodiesel involves treating biodiesel raw oil including lower fatty acid having acid value of 20 mg potassium hydroxide/g or less with an adsorbent to remove impurities phase, dehydrating the treated oil to remove foreign substance, removing metal cation from the raw oil using cation exchange resin, reacting the resultant raw oil in presence of solid acid catalyst, mixing obtained raw oil with methanol, carrying out esterification reaction, and reacting the obtained product in presence of alkaline catalyst.    USE - Manufacture of biodiesel (claimed).    DETAILED DESCRIPTION - Manufacture of biodiesel involves treating biodiesel raw oil including lower fatty acid having acid value of 20 mg potassium hydroxide/g or less with an adsorbent to remove impurities phase, dehydrating the treated oil to remove foreign substance, removing metal cation from the raw oil using cation exchange resin, reacting the resultant raw oil in presence of solid acid catalyst at 20-80 degrees C in a guard bed reactor with reaction volume of 6 vol.%, mixing obtained raw oil with methanol, and carrying out esterification reaction at 70-120 degrees C under flow rate of 0.5-1.5 SV to obtain product having acid value of 5 mg potassium hydroxide/g or less, and reacting the obtained product in presence of alkaline catalyst.
NOVELTY - The natural ignition briquet has multiple circular form globes (2) that are filled with the palm oil or paraffin buried in a portion of the outer cover. Multiple ventilation holes (11) are formed along the side circumference of the round rod (1). The lower unit of the round rod is formed with groove. The shell of bamboo is peeled off at the constant interval.    USE - Natural ignition briquet for use in home.    ADVANTAGE - The stage firing in circular form outlet is facilitated and the filled round rod is burnt for the long time. The penetration of the contaminant in the igniting briquette can be easily discharged using bamboo and coconut in the palm oil or paraffin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing natural ignition briquette.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the natural ignition briquette.    Round rod (1)    Circular form globes (2)    Ventilation hole (11)
NOVELTY - Preparing bio-organic fertilizer includes fermenting raw material with microorganism and uniformly mixing to obtain the mixed material, where the carbon to nitrogen ratio of the mixed material is controlled at 15-40:1, and the water content is adjusted to 50-60 pts. wt. by adding water plant or animal protein to the mixed material; and fermenting mixed material to obtain the fermented bio-organic fertilizer.    USE - Method for preparing bio-organic fertilizer (claimed).    DETAILED DESCRIPTION - Preparing bio-organic fertilizer comprises fermenting raw material with microorganism and uniformly mixing to obtain the mixed material, where the carbon to nitrogen ratio of the mixed material is controlled at 15-40:1, and the water content is adjusted to 50-60 pts. wt. by adding water plant or animal protein to the mixed material; and fermenting mixed material to obtain the fermented bio-organic fertilizer, where the raw material comprises 700-800 pts. wt. dry Pleurotus eryngii bacteria slag, 10-50 pts. wt. wheat bran, 10-50 pts. wt. rice bran, 0-10 pts. wt. brown sugar, 0-10 pts. wt. cane sugar, 0-10 pts. wt. other natural inorganic mineral rock, 30-60 pts. wt. mineral powder, 20-50 pts. wt. plant ash, 0-50 pts. wt. borax, 0-20 pts. wt. mineral powder, 0-50 pts. wt. sulfur, 0-30 pts. wt. gypsum or 0-40 pts. wt. lime stone. The microorganism of solid state fermentation comprises 0.2-10 pts. wt. effective viable count which is more than 5000 per g of Bacillus subtilis, 0.2-10 pts. wt. effective viable count which is more than 5000 thousand per gram of yeast, 0.2-10 pts. wt. effective viable count which is more than 5000 thousand per gram of Trichoderma, 0.2-10 pts. wt. effective viable count which is more than 5000 per g of phosphorus, 0.2-10 pts. wt. functional bacteria effective viable count which is more than 5000 per g of potassium, and 0.2-10 pts. wt. functional bacteria effective viable count which is more than 5000 thousand per gram of bacteria.
NOVELTY - Use of 2 alpha ,3 beta -dihydroxyolean-13(18)en-28-oic acid or its salt in the preparation of an antibacterial agent, is claimed.    USE - The 2 alpha ,3 beta -dihydroxyolean-13(18)en-28-oic acid or its salt is useful in the preparation of an antibacterial agent for combating gram-positive bacteria, preferably Staphylococcus aureus or Bacillus thuringiensis or a gram-negative bacteria, preferably Escherichia coli, Salmonella or Shigella dysenteriae in fruits and vegetables (all claimed). The fruit is useful in the preparation of 2 alpha ,3 beta -dihydroxyolean-13(18)en-28-oic acid (claimed).    ADVANTAGE - The 2 alpha ,3 beta -dihydroxyolean-13(18)en-28-oic acid produces antibacterial agent which is rich in plant source, and has broad spectrum antibacterial activity, and high bacteriostatic activity, and is safe for foods e.g. fruits and vegetables. The method has easy extraction procedure; utilizes plant fruit extract which do not decay and can be utilized for a longer period; is environmental friendly, and economical; and produces product with good stability, monomeric compounds and easy storage capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing 2 alpha ,3 beta -dihydroxyolean-13(18)en-28-oic acid, comprising extracting Rosa laevigata Michx. fruit.
NOVELTY - Cultivation of mushroom comprises taking 1 wt.% cinnamon sawdust in water at ratio of 1:1.5, mixing with lime in fermentation tank, fermenting at 60-65 degrees C for 4-5 days, carrying out aeration, adding 25 wt.% wheat bran and 2% calcium carbonate to 73 wt.% fermented product, mixing, controlling moisture content at 65-70%, sterilizing, applying and cultivating.    USE - Method for cultivating mushroom (claimed).    ADVANTAGE - The method is low-cost and environment-friendly.
NOVELTY - Solar greenhouse warming comprises collecting crop straw, crushing into 3-5 cm long, adding 35 wt.% water, placing in bags and keeping in greenhouse shed.    USE - Method for solar greenhouse warming (claimed).    ADVANTAGE - The method is low-cost and environment-friendly.
NOVELTY - Biological fertilizer comprises 65-80 pts. wt. concentrated molasses fermented liquid, 7-14 pts. wt. humate, 0.5-2 pts. wt. chelated microelement, 1-5 pts. wt. strain and 5-10 pts. wt. surfactant, where the chelated microelement is mixture of EDTA-copper, EDTA-iron, EDTA-manganese and EDTA-zinc, and where the strain is chosen from Paenibacillus polymyxa, Bacillus subtilis and B.mucilaginosus.    USE - The biological fertilizer is useful for improving the growth of crops including grain, vegetable, melon and other fruits.    ADVANTAGE - The biological fertilizer is environmentally-friendly, improves soil environment and increases crop yield to 10-20%.
NOVELTY - This utility model claims a pure water manufacturing system to pure hydrogen, belonging to the hydrogen preparation field. This utility model of the anode wiring terminal of the electrolytic cell, the cathode wiring terminal and the direct current source is connected with the oxygen outlet is connected to the water tank, the lower part of the water inlet port and the water tank is connected with the hydrogen outlet is connected to the gas-liquid separator, the gas-liquid separator at the bottom of the return joint is connected to the water tank, the gas outlet of the gas-liquid separator is connected with the first level dryer, a dryer, a dryer outlet is orderly connected with a four-way, three-way, four-way is connected with the over-voltage protection element and a pressure gauge, three-way is connected with a flow sensor, the outlet of the tee joint is connected with a flow control valve, the said direct current power supply, a over-voltage protection element, a flow sensor, a pressure meter are connected with the control system; The utility model is provided with over-voltage protection and a water level control dual-protection function, which greatly improves the security of the system, the hydrogen production efficiency is high, the purity is as high as 99.999% or more.
NOVELTY - This utility model claims a kind of organic solid waste resource ferment device, wherein it comprises a vertical, the top of the vertical chamber is provided with feeding port and an exhaust port, the bottom is provided with a spiral discharge device and a discharge hole, inner part is provided with a stirring device and air distributing pipe, cloth wind pipe with the Roots fan is connected with the bin body, the pipeline is connected with the exhaust fan. This utility model not only shortens the time required to harmless treatment, reducing nutrient loss, improve the product fertilizer effect, and ferment under the aerobic condition, which effectively avoids the malodorous gas, so as to reduce the pollution to the environment, and can realize automatic feeding and automatic discharging, reduces the labour intensity.
NOVELTY - Sheep farm excrement treatment system comprises a solid-liquid separator of excrement device, an adjusting pool, a pre-processing manure shed, a fermentation manure shed, liquid manure conveying pipe and a biogas digester.    USE - The system is useful for producing biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating sheep farm excrement, comprising pre-processing the excrement in a solid-liquid separator, conveying the solid waste into a compost fermenting site, then conveying into an organic fertilizer factory after fermentation, adding some components to form an organic fertilizer, conveying the liquid excrement into a biogas fermentation tank through a pipeline system, and utilizing the biogas fertilizer by farmers for irrigating the land nearby.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sheep farm excrement treatment system (Drawing includes non-English language text).
NOVELTY - A bortezomib intermediate is prepared by performing condensation reaction to (1S,2S,3R,5S)-pinanediol-L-phenylalanine-L-leucine boric acid ester salt and pyrazine-2-formate in the presence of condensing agent and organic solvent.    USE - Preparation of bortezomib intermediate (claimed).    ADVANTAGE - Preparation method is simple and environment-friendly, has high yield and mild reaction conditions, eliminates use of organic alkali, and reduces cost.    DETAILED DESCRIPTION - A bortezomib intermediate of formula (I) is prepared by performing condensation reaction to (1S,2S,3R,5S)-pinanediol-L-phenylalanine-L-leucine boric acid ester salt of formula (II) and pyrazine-2-formate of formula (III) in the presence of condensing agent and organic solvent.    X=acid; and    M+=cation.
NOVELTY - A kind of marsh gas engineering product and agricultural planting are combined with a comprehensive utilization system, comprising a producing marsh gas by anaerobic fermentation tank is provided with a pipeline and a pipeline irrigating system for multiple crop planting land, anaerobic fermentation liquid in the fermentation tank of the upper layer separating the biogas stored in the biogas pool, and then flow through the pipeline valve of crop planting irrigation system in the anaerobic fermentation tank top layer of the marsh gas after desulfurizing process by desulphurization device for supplying combustion gas generator, the gas generator of the circulating cooling water and high temperature flue gas waste heat absorption and for anaerobic reaction liquid in the fermentation tank for heat preservation is heat and power generation device, and a secondary heat exchange medium temperature flue gas after cooled by the cooling device is composed of a gas valve in a gas pipeline in the pipeline of the crop planting irrigation system. Crop planting area and marsh gas engineering product yield is the number matched and respectively to produce marsh gas engineering realization is a product of the largest value, crop planting is realized and the largest planting efficiency.
NOVELTY - Trimethylene sulfide is used as hydrate accelerant.    USE - Trimethylene sulfide used as hydrate accelerant (claimed).    ADVANTAGE - The accelerant is recyclable and has hydrate formation rate of 0.1-0.5 mol/min/m3.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of trimethylene sulfide for preparation of hydrate comprising adding trimethylene sulfide to water at 5-30 degrees C and 0.01-5.0 MPa, and introducing reaction gas, and fully mixing.
NOVELTY - A linkage efficient biogas plant comprises reactor upflow gas tank (11), plug-flow digesters (20), a methane gas export pipeline (22), and a gas outlet pipe (2).    USE - A linkage efficient biogas plant.    ADVANTAGE - The plant does not need additional building biogas storage cabinet.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the plant.    Gas outlet pipe (2)    Reactor upflow gas tank (11)    Plug-flow digesters (20)    Gas chamber (21)    Methane gas export pipeline (22)
NOVELTY - The method involves providing a kettle with a FCC waste catalyst material and a black rosin raw material. A rosin biological diesel oil raw material is formed with a cooling layer and a filtering layer. Temperature range of a roasting layer and an impregnation part is about 500 to 760V centigrade and 60 to 100 degrees centigrade. Mass ratio of a liquid-solid is about 5: 1. The catalyst material is filled with hydrochloric acid, sulphuric acid, nitric acid, citric acid, phosphoric acid, oxalic acid, boric acid, acetic acid or benzene sulfonic acid. Protective gas is mixed with CO2 or N2.    USE - FCC waste catalyst load black rosin acid and catalytic cracking biological diesel oil preparing method.    ADVANTAGE - The method enables improving economic benefit and environment benefit, and reducing energy consumption.
NOVELTY - The system has a storage bin storing biomass fuel. A spiral conveyor is provided with a gasification furnace. A secondary gasification reaction tower is provided with a cyclone separator that is used for removing ash. Biomass fuel gas is generated by a heating furnace. A smoke exhaust pipeline outlet is connected with a heat boiler. Water steam is generated by the gasification furnace using air-steam gasification reaction.    USE - Biomass water vapor gasification heating system.    ADVANTAGE - The system improves flow amount and thermal value of the biomass fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass water vapor gasification heating system.'(Drawing includes non-English language text)'
NOVELTY - This utility model claims one kind of sorghum solid continuous distillation device for preparing ethanol, said solid continuous distillation device is composed of a feeding packing auger, a bucket elevator, a distillation kettle, a steam chamber, steam collecting pipe, a cooler, a discharging device. The sweet sorghum solid continuous distillation device is for preparing fuel ethanol for sweet sorghum solid ferment and practical one process model. By continuous distillation and can greatly improve the labour efficiency and saves energy. In order to realize solid fuel ethanol production scale, high degree of automation; So as to better popularization of promoting biological energy technology.
NOVELTY - The utility model claims one based on DCS's 97 # methanol gasoline blending system comprises methanol component adjustment system and a gasoline component adjusting system, the methanol component adjustment system and a gasoline component adjusting system through the pipeline mixer, the mixer is connected with a finished product tank or methanol gasoline oil pipeline, said methanol component adjustment system and a gasoline component adjusting system are electrically connected with the control system by DCS. The beneficial effect is that the proportion by DCS system can conveniently's preparing methanol component adjusting and gasoline component's, the different component ratio's the second time preparing into gasoline's to gasoline component and component, made's methanol gasoline with methanol, the adjusting component proportion preparing high can satisfy the gasoline blending component's different.
NOVELTY - The utility model claims one based on DCS's 93 # methanol gasoline blending system comprises methanol component adjustment system and a gasoline component adjusting system, the methanol component adjustment system and a gasoline component adjusting system through the pipeline mixer, the mixer is connected with a finished product tank or methanol gasoline oil pipeline, said methanol component adjustment system and a gasoline component adjusting system are electrically connected with the control system by DCS. The beneficial effect is that the proportion by DCS system can conveniently's preparing methanol component adjusting and gasoline component's, the different component ratio's the second time preparing into gasoline's to gasoline component and component, made's methanol gasoline with methanol, the adjusting component proportion preparing high can satisfy the gasoline blending component's different.
NOVELTY - This utility model claims one kind of biological diesel oil processing device, comprising a diesel tank, additive tube, regulator tank and reaction kettle, said kettle comprises's mixing tank, a stirring tank and a finished product tank, said stirring tank and the finished product tank is further provided with connected with each other's pulse mechanism, ultrasonic generator and magnetic jar, and said pulse mechanism 4 with the stirring tank, said magnetic jar with the finished product tank. The utility model is provided with the stirring tank in the reaction kettle taking one mechanical stirring, and by the pulse mechanism, ultrasonic generator and magnetic jar taking the secondary mixing, improves the reaction's stirring strength, so as to improve the production efficiency and yield.
NOVELTY - A hydrogen steam sprayer, comprising one base, one is set on the supporting frame and hydrogen said vapour generating chamber, the bottom of the base part extends outward from the base of one pipe body, one spraying cover is set on said tube body end of the cabin is set in the through hole of the spray cover, said gas steam generating is provided with an electrode plate, said base is provided with said electrode plate is connected, the circuit is connected with one external power supply line. The utility model is obtained by electrolyzing water for steam cosmetic, it has simple structure and convenient use. high grade
NOVELTY - The device comprises a gas-water separator comprising an upper shell and a lower shell, an air inlet pipe, a drain pipe, and an exhaust pipe. The upper and lower shells are connected with each other through a flange, and are provided with an O-shaped sealing ring. The upper shell corresponding to the exhaust pipe is provided with an exhaust box. The exhaust box is provided with a valve body sealing ring, and an air outlet valve spring. The lower shell corresponding to the air inlet pipe is provided with a filter medium. The lower shell and the drain pipe are provided with a drain tank.    USE - The device is useful for generating hydrogen (claimed).    ADVANTAGE - The device has simple structure and improved operational efficiency, is easy to use, and enables energy-efficient generation of hydrogen in an environmentally friendly manner.    DETAILED DESCRIPTION - The device comprises a gas-water separator comprising an upper shell and a lower shell, an air inlet pipe, a drain pipe, and an exhaust pipe. The upper and lower shells are connected with each other through a flange, and are provided with an O-shaped sealing ring. The upper shell corresponding to the exhaust pipe is provided with an exhaust box. The exhaust box is provided with a valve body sealing ring, and an air outlet valve spring. The lower shell corresponding to the air inlet pipe is provided with a filter medium. The lower shell and the drain pipe are provided with a drain tank. The drain tank is provided with upper and lower limit sealing rings. The upper and lower sealing rings are inserted in a drain valve body.
NOVELTY - A meat carcass pyrolysis processing device contains pyrolysis chamber (1), combustion chamber (2), and biomass burner (3) in which biomass burner and combustion chamber is provided with flue gas inlet, provided between pyrolysis chamber and combustion chamber is gas outlet, pyrolysis tank is located inside pyrolysis chamber, pyrolysis tank is provided with baskets, basket rail, and pyrolysis outlet pipe, 1st end of pyrolysis outlet pipe is connected with pyrolysis tank and next end is connected with combustion chamber, and pyrolysis chamber is provided with rows of chimney (7).    USE - A meat carcass pyrolysis processing device (claimed).    ADVANTAGE - Device is highly efficient and rational, shortens processing period, improves pyrolysis effect, and has high energy utilization rate.    DETAILED DESCRIPTION - A meat carcass pyrolysis processing device contains pyrolysis chamber (1), combustion chamber (2), and biomass burner (3) in which biomass burner and combustion chamber is provided with flue gas inlet, provided between pyrolysis chamber and combustion chamber is gas outlet, pyrolysis tank is located inside pyrolysis chamber, pyrolysis tank is provided with baskets, basket rail, and pyrolysis outlet pipe, 1st end of pyrolysis outlet pipe is connected with pyrolysis tank and next end is connected with combustion chamber, pyrolysis chamber is provided with rows of chimney (7), pyrolysis tank is provided with open or close pyrolysis tank door (8), pyrolysis chamber is provided with cooling chamber (9), cooling chamber is provided with baskets adapted to cooling tank, and pyrolysis chamber is greater than or equal to 1.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of meat carcass pyrolysis processing device.    Pyrolysis chamber (1)    Combustion chamber (2)    Biomass burner (3)    Chimney (7)    Pyrolysis tank door (8)    Cooling chamber (9)
NOVELTY - The method involves mixing non-dehydrated crude oil and water according to mass ratio of 100:1 to 200:1. The mixed crude oil and water is fed to a fractionating tower to generate vapor, where tower top temperature of the fractionating tower is maintained at 80-90 degrees Celsius and tower top pressure of the fractionating tower is 0.15-0.20 MPa. The vapor is entered to a condenser. Condensed water is separated. Gasified liquid phase high-temperature crude oil is heated in a reboiler. Qualified crude oil is separated by a crude oil buffer tank after dehydration process.    USE - Steam condensed water stripping crude oil stabilizing method.    ADVANTAGE - The method enables ensuring low energy consumption, improving processing efficiency of a steam condensed water stripping crude oil stabilizing device, effectively increasing stable efficiency crude oil collection rate during light hydrocarbon production and maintaining water content in the crude oil without need of filling auxiliary agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a steam condensed water stripping crude oil stabilizing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a steam condensed water stripping crude oil stabilizing device.
NOVELTY - The utility model claims one electrolytic water for preparing hydrogen and oxygen's system, comprising one first sedimentation tank, medicine adding device A, agent A, agent B and stirring device, stirring device, B, a secondary sedimentation tank, a resin filter, an RO reverse osmosis water purifying machine, a pure water storing pool and water electrolysis device, the utility model's advantages are (1) the utility model, on the one hand, low cost for processing the urban sewage, on the other hand, is an electrolytic water hydrogen and oxygen supplying water resource, saves a lot of water resource. (2) using this utility model each sewage processing 10000 ton's at the same time, producing hydrogen about 308 ton, reduces the discharging amount of carbon dioxide 7675, reduces the discharge amount of sulfur dioxide 92, reduces the dust emission 1642 and so on.
NOVELTY - A one sludge low temperature hot tempering anaerobic biogas complete processing device, comprising a sludge storing and conveying device, a sludge low temperature hot tempering device, a sludge anaerobic digestion device, hot exchange device, waste gas processing device, a sludge hot exchange storage device, a mechanical dewatering device, deodorizing device and steam boiler is a supercritical boiler. The security's the device is high, the whole reaction process has no dust, no electrostatic explosion potential safety hazard, high efficiency, saves the energy consumption, the whole process effectively recycle hot energy recycle for many times, which is good for saving energy consumption, and environment-friendly and can reuse.
NOVELTY - One lower-suction type straw fuel gas hot source machine fundamentally solves the straw gas generator up circulating water heating efficiency is low, the problem's energy waste. Comprising a water jacket's fuel gas generator and gas separating box, the mixed gas inlet of the mixed gas outlet of the gas separating box's's fuel gas-generating stove, the technical solution is as follows: said fuel gas generator is an integrated structure, comprising a feeding port's upper hearth and lower hearth combustion chamber and the ash's water pipe type fire grate and the water jacket is connected with the separated's's, gas separating box by the clapboard is divided into purifying chamber and the cooling chamber, cooling box's circulating cooling water in the cooling chamber, the upper cooling box is provided with a cooling tank water inlet pipe with the cooling tank, purifying by purification cabin vertical plate is divided into purifying gas passage with the purifying chamber. To double-heating water pipe is transversely connected with the water pipe and the fire grate heating pipe target design, this utility model adopts the combustion layer filtering opening filler, the fuel gas;
NOVELTY - This utility model claims one kind of oil-saving and emission reduction device, comprising a shell, wherein the shell is equipped with electrically connected with the generator's multi-pole plate through electrolysis water device and the multi-pole plate electrolytic water's device is connected with the gas-water separating tank, the top end of the gas-water separating tank's opening and is provided with a sealing cover, a gas-water separating tank's upper end can be connected to gas outlet's upper inlet up the opening. The utility model passes through the electrolytic water's oxygen mixed gas into the engine, so as to improve the fuel efficiency and reduces the discharge of harmful gases, and at the same time, the multi-pole plate's water electrolysis device has simple structure, convenient control and electrolytic water efficiency is high.
NOVELTY - An air quantity adjusting valve's one of straw gasification furnace, it has one upper one is shape's four-way valve body, the bottom of upper vertical tube's the four-way valve body is provided with one valve core, the horizontal pipe and the vertical pipe is provided with one adjusting screw, said valve core and the adjusting screw is set with one pressure spring, at the same time, one end of the horizontal pipe is provided with one's fire switch, top part's vertical pipe is provided with a valve switch. The design of this utility model is reasonable, the structure is simple, it can distribution quantity's air supply amount and distribution air boxes according to the combustion state's state's gasification furnace gasification furnace and gasification furnace's head adjusting to obtain the ideal gasification effect and burning effect.
NOVELTY - The utility model claims one civil saving firewood and coal multipurpose furnace, a hearth and upper part is front furnace opening, furnace upper part one side of the gasification chamber, a gasification combustion chamber is provided with a through kang smoke outlet, cooking gasification combustion chamber is set above the furnace's front opening's upper furnace is one of biomass fuel storage box, the lower end is provided with a storage tank's fire grate is connected with the hearth, storage tank is provided with a jacket, the jacket's outer layer is provided with a water replenishing opening and adjustable air inlet's, the jacket's inner layer is arranged with multiple small air storage tank connected's. The hearth can be coal or firewood or the two are mixed, to form small's vaporizing burner of biomass fuel, the biomass fuel into the combustible gas in the hearth and the combustion without black smoke, hot efficiency is high, which greatly saves the fuel's consumption, can meet the household cooking or other hot energy's life.
NOVELTY - Invention relates to a device for briquetting of biowaste of animals and birds, comprising a loading hopper, a conical auger installed in the hollow body, a scraper conveyor arranged in the lower part of the body, a spring-loaded plate in the form of a ski is installed at the side of the conical auger top at the outlet from the body. It additionally comprises a mixer made of a body, nozzles for input of a filler and an aggregate, besides, along the vertical axis of the mixer body there is a rotor with blades arranged at the angle to each other, the lower part of the mixer via the gate and the pipeline is connected to the lower part of the device for mixing of the material with the binder made of a body and a nozzle of binder injection, inside the body on its opposite sides there are two augers in the form of a spiral with the opposite winding rotating with the help of electric motors, at the outer side of the device body for mixing along its perimeter there is a coil with a coolant. Blades installed on the rotor of the mixer have the shape of a rectangular triangle. Application of the proposed device makes it possible to use biowaste of animals (manure, dung), and also to use local resource in the form of easily available and environment-safe materials.    USE - Power engineering.    ADVANTAGE - Produced briquettes are used for heat production.2 cl, 1 dwg
NOVELTY - The method involves increasing the bus unit voltage in bus unit, till the final target value is progressed. Determination is made whether the abnormality of the bus unit is increased. The first voltage boosting time is set up till the bus unit voltage is progressed. Determination is made whether the battery state is in normal condition. The pre-charging function of the boost converter is implemented by software algorithm process, to start the fuel cell vehicle without the additional hardware configuration.    USE - Method for controlling boost converter.    ADVANTAGE - Since the fuel cell vehicle is started using low voltage battery, the abnormality of the bus unit is determined in the first step-up and the second step-up is not issued when the problem in the vehicle is ideal, Thus the permanent damage of the boost converter can be prevented without the additional hardware configuration. The cost reduction can be achieved due to the deletion of the pre charge relay, and the component number reduction can be achieved and thus the trouble danger factor reduction can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process for controlling boost converter. (Drawing includes non-English language text)
NOVELTY - A tartrate methanation catalyst is prepared by mixing dispersing agent and 20-30 wt.% catalyst, putting into planetary ball mill for 20-40 minutes, adding tartaric acid solution and auxiliary agent M, drying at room temperature for 24 hours, heating at 110 degrees C for 2-4 hours, calcining at 400-600 degrees C for 4-6 hours, and cooling to room temperature.    USE - Method for preparing tartrate methanation catalyst (claimed).    ADVANTAGE - The method is energy efficient.
NOVELTY - A biodiesel esterification composite acid catalyst comprises acid and corrosion inhibiting agent composition at ratio 1:0.01-0.15. The acid is methanesulfonic acid, ethanesulfonic acid, or chlorosulfonic acid. The corrosion inhibiting agent is phosphoric acid monoester, polyether acid phosphate, or propargyl alcohol.    USE - Biodiesel esterification composite acid catalyst.    ADVANTAGE - The catalyst has high catalytic activity, less dosage in biodiesel esterification, no by-product, and high catalytic efficiency, and does not easily separates product.
NOVELTY - Apparatus comprises four operation assemblies connected to each other, a material feeding unit including feeding head, inlet, feeding duct, feeding bulb and forced feeding support tool; an anaerobic fermentation tank unit including anaerobic fermentation chamber, gas containing chamber, forced skimmer and biological skimmer; an outlet-regulating tank unit including outlet, fender, elevation chamber, regulating tank, convolution gate and discharge pipe; and a waste fluid treatment unit including waste fluid containing tank and waste fluid drying treatment tank.    USE - As an apparatus for producing biogas from agricultural waste products, biomass and organic household wastes (claimed).
NOVELTY - A one garbage processing, preparing fertilizer integrated machine, comprising a feeding hopper, a belt conveyor, a plastic blowing machine, a magnetic separator, a sieving machine, a crusher, a machine for making soy by saltless ferment part, the left end is provided with a feed hopper's the integrated machine, a feeding hopper's side is set between plastic blowing machine, a feeding hopper and the plastic blowing machine material inlet through the first belt conveyor is connected with the side's plastic blowing machine is provided with a magnetic separator, separator is provided with a sieving machine's between the discharge hole is connected with the sieving machine's machine the plastic blowing material's magnetic separator is provided with a second lower belt conveyor, sieving machine is set up with organic and inorganic material outlet, the material outlet side's machine is provided with a crusher, the feeding port's organic material outlet of the crusher is set between the third belt conveyor, crusher is provided with a fermenting's organics. Crusher's discharge hole is connected with the fermenting machine's between the port is provided with a fourth belt conveyor.
NOVELTY - Synthetic ammonia/methanol treatment system comprises heat exchanger (1), heater (3), converting furnace (2), emptying tail gas pipeline (7), oxygen pipeline (5), and superheated steam pipeline (4).    USE - Synthetic ammonia/methanol treatment system.    ADVANTAGE - The system saves energy and reduces emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the system comprising preheating tail gas and oxygen with superheated steam at 500-700 degrees C, sending into converting furnace, reacting, and sending into heat exchanger to obtain reformed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of synthetic ammonia/methanol treatment system    Heat exchanger (1)    Converting furnace (2)    Heater (3)    Superheated steam pipeline (4)    Oxygen pipeline (5)    Emptying tail gas pipeline (7)
NOVELTY - A nano photothermal conversion material comprises molybdenum oxide. The nanomaterial is nanosphere, nanobelt, nanorod, or nanowire.    USE - Nano photothermal conversion material used for cancer treatment.    ADVANTAGE - The material is simple to prepare. Preparation method is environment-friendly and has low cost.    DETAILED DESCRIPTION - A nano photothermal conversion material comprises molybdenum oxide of formula MoO3-x. The nanomaterial is nanosphere, nanobelt, nanorod, or nanowire.    x=0-1.    An INDEPENDENT CLAIM is included for preparation of nano photothermal conversion material by adding hydrogen peroxide (H2O2) to molybdenum, stirring, and diluting to 100 ml to obtain precursor solution; and adding surfactant to the precursor solution, uniformly stirring, hydrothermally reacting at 50-300 degrees C for 1-48 hours, and centrifuging. The volume-weight ratio of H2O2 and molybdenum is 0-100:0.1-1000. The weight-volume ratio of surfactant and precursor solution is 0.01-1000:0.1-100.
NOVELTY - Melting and evaporating lignin-, cellulose-, and/or carbonaceous material streams, comprises forming a closed and interconnected unit with a drier, a filling device, a pyrolysis reactor and conducting heat and electricity together with material flow in moderately energetic manner introducing the combustion gases through a wet product-inlet, and discharging of the solids using hot gases and the wet steam.    USE - The method is useful for melting and evaporating lignin-, cellulose-, and/or carbonaceous material streams.    ADVANTAGE - The method is cost efficient and recycles the energy utilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above mentioned method, where material transport takes place in the reactor by a conveyor from screw paddle, which extends over the entire pitch length of the heated evaporation reactor.
NOVELTY - The hydrogen generator has a composite electrolytic cell with membrane electrodes. The solid polymer electrolyte is polarized to generate hydrogen from water at a cathode and oxygen at an anode. The membrane electrode assemblies (1,17) divide the interior of the hydrogen generator into three successive chambers (12,11,23). The external supply of liquid water is supplied to a chamber bounded by the anode surface of a membrane electrode assembly. The cathode surfaces of membrane electrode assemblies face each other in a common chamber, such that cathodes generate hydrogen in the common chamber.    USE - Hydrogen generators for generating dry hydrogen.    ADVANTAGE - The hydrogen generator has a composite electrolytic cell with membrane electrodes, thus reduces the water throughput from the primary generator, and hence increases the efficiency on a hydrogen electrolyser. The solid polymer electrolyte is polarized to generate hydrogen from water at a cathode and oxygen at an anode, thus prevents passage of water droplets from one location to another.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of generating dry hydrogen by electrolysis of water in a composite electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator in which hydrogen is dried by a two cell configuration sharing a common gaseous chamber and a sectional view of a membrane electrode assembly.    Electrode assemblies (1,17)    Water (2)    Electrolyte (2a)    Chambers (12,11,23)    Threaded sections (25)
NOVELTY - Preparation of fragrant carbon adhesive comprises mixing 15-25 pts. wt. tapioca and 40-60 pts. wt. flour to obtain mixture; adding 1000-1200 pts. wt. water to reaction vessel, and heating to 60-80 degrees C; adding 10 times water to mixture, slowly pouring into heated water, continuously heating to 80-100 degrees C, adding 8-12 pts. wt. sodium carbonate, 6-10 pts. wt. carboxymethyl starch, and 8-12 pts. wt. guar gum, stopping heating, adding 1-3 pts. wt. sandalwood powder, and stirring to carry out dispersion.    USE - Method for preparation of fragrant carbon adhesive (claimed).    ADVANTAGE - The adhesive has woody aroma.
NOVELTY - And the utility model belongs to a kind of coal pyrolysis with a garbage organic waste to a reaction kettle, the reaction kettle rotate inside the stirring conveyer to prevent coking material is heated to produce the material causes the blockage and is suitable for a, domestic waste, sludge, waste plastic, waste rubber, thermal treatment of biomass waste, comprising a reaction kettle wall is not coking, no deformation, good sealing property, high yield, does not comprise a gas product, the thermal value is high, it is not generating a in the production.
NOVELTY - Production of liquid organic fertilizer comprises combusting biomass residue and slag water, adding organic acid, adjusting pH to 5-8, concentrating at mass ratio of 3-30:1, and filtering; or combusting biomass residue and slag water, concentrating at mass ratio of 3-30:1, filtering, adding organic acid to filtrate, and adjusting pH to 5-8. The organic acid is alginic acid, amino acid, glutamic acid, citric acid, or humic acid.    USE - Method for producing liquid organic fertilizer (claimed).    ADVANTAGE - The method solves water pollution problem.
NOVELTY - This utility model claims a kind of organic fertilizer production field, especially relates to a kind of organic fertilizer fermenting system. The system comprises a gas supply system and a fermenting pool. The gas supply system comprises a freezing drier, a pressure gauge water filter and a heating band. The heating band is installed on a pipeline which connects the freezing drier and the pressure gauge water filter. The bottom wall of the fermenting pool comprises a vertically arranged metal strip and is provided with a groove. A guide rail is arranged at the upper edge of the fermenting pool. A seepage pipe of the gas supply system is installed in the groove. Rollers are installed at both ends of a framework of a mobile plastic shed and slide in the guide rail. Two traction slide wheels are installed outside the framework at both ends. A traction ring is installed inside the framework and is connected through a nylon rope. The beneficial effect of the utility model lies in: when at the same time the leavening ferment time is also does not need turning fermentation product, at the same time, ensures the following to a fermentation temperature in different weather, at the same time improves the production efficiency and effectively saves energy.
NOVELTY - The method involves delivering energy from energy source. The wind energy converted into electrical energy is supplied to the electrolyzer. The electrolyzer is provided for realization of electrolysis of water supplied from the container. The obtained result of electrolysis of water is supplied into hydrogen accumulator and oxygen accumulator. The heat pump is provided to heat the water. The hot water is sent to the hot water supply pipe or storage unit for use by user.    USE - Method for producing hydrogen from water based on energy source.
NOVELTY - Method of producing hydrocarbon propellants involves combined drying and cleaning of hydrocarbon material and separating the hydrocarbon propellant composition. The hydrocarbon material used is propane, a butane fraction or isobutane or n-butane or propane or a mixture of propane and n-butane. Drying and cleaning is carried out by passing the material in liquid-phase through sorbents in three series-arranged adsorbers. The first adsorber on the process path is filled with aluminium oxide, the second adsorber is filled with zeolite NaA and the third adsorber is filled with zeolite NaX. The given propellant composition is obtained after the third adsorber, wherein if the hydrocarbon material used is a mixture of propane and n-butane, the given propellant composition is obtained in a mixer by mixing propane and n-butane in weight ratio of 0.96.    USE - Chemistry.    ADVANTAGE - Obtaining a product of high quality with low content of moisture and sulphur compounds, low operational and capital costs on implementing the process.2 dwg, 1 tbl
NOVELTY - Invention propose a strain of Chlorella vulgaris IPPAS C-616 microalgae for obtaining lipids as raw material for production of motor fuel.    USE - Biotechnologies.    ADVANTAGE - Strain of microalgae has an ability to produce lipids with high content of saturated and mono non-saturated fatty acids.1 dwg, 1 tbl, 3 ex
NOVELTY - The cutting apparatus (100) has a holding portion that holds non-cutting portion of laminated film (LB). A press portion (112) and adsorption stand (124) are provided to pinchingly support cutting portion of film in a position adjoining a direction along surface of holding portion and film. The non-cutting portion of film currently held at holding portion is spaced apart from cutting portion of film so that the cutting and non-cutting portions of film are separated, while the press portion and adsorption stand are made to pinchingly support the cutting portion of film.    USE - Cutting apparatus used for cutting laminated film used for manufacturing fuel cell (all claimed) such as polymer electrolyte fuel cell.    ADVANTAGE - The cutting and non-cutting portions of film can be separated and the film can be cut, using the retention strength and pinching support force of press portion and adsorption stand, and holding portion, and without using the cutting blade. Therefore, the fall of the cutting precision resulting from abrasion of the film contacting the cutting blade can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cutting method of electrolytic membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the operation of the cutting apparatus.    Cutting apparatus (100)    Punch portion (111)    Press portion (112)    Adsorption stand (124)    Laminated film (LB)
NOVELTY - A raw material which adjusts the mix ratio of organic waste and a refuse paper and plastic fuel manufacturing raw material is mixed with respect to content rate of moisture content contained in organic waste. The raw material is molded from the mixing raw material, to obtain solid fuel.    USE - Manufacture of solid fuel (claimed).    ADVANTAGE - The solid fuel is easily and efficiently manufactured with hard to generate offensive odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of processing flow.    Drying machine (1)    Mixer (2)    Molding machine (3)    Sludge (11)    Organic waste (12)
NOVELTY - The system has a catalytic oxidizer (220) which supplies the reformate gas from a reformer (130) in the initial awakened mode. The reformer allows the gas provided in the initial electricity mode and fuel in the initial awakened mode, while distributing the electricity produced in the fuel cell stack (210). A power control unit (310) controls generation of the energy fed for starting the fuel cell stack. The fuel cell stack initiates the electro chemical reaction of the fuel gas to generate electricity to the fuel cell (200).    USE - Singleness starting system of marine fuel cell.    ADVANTAGE - The electricity for starting the fuel cell can be triggered effectively without the separate generator, so that energy consumption of the fuel cell can be enhanced. The reformate gas in the initial awakened mode of the fuel cell can be reduced effectively. The initial move electricity needed for the moving the fuel cell can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the singleness starting system. (Drawing includes non-English language text)    Reformer (130)    Fuel cell (200)    Fuel cell stack (210)    Catalytic oxidizer (220)    Power control unit (310)
NOVELTY - A denitration catalyst comprises ultramicropore alumina as a carrier and catalytically active copper oxide.    USE - Denitration catalyst.    ADVANTAGE - The preparation is simple, low cost and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of denitration catalyst comprising dissolving organic acid and inorganic acid in not greater than 95 vol.% ethanol, adding salt, aluminum-containing solution and surface active agent, stirring at 20-60 degrees C for 6-24 hours, transferring to petri dish, maintaining at 30-80 degrees C for 48-72 hours, calcining at 400-800 degrees C for 5-10 hours, and carrying out selective catalytic reduction (SCR) flue gas denitrification at 400 degrees C.
NOVELTY - Removing organic phosphorus in sewage comprises: pretreating photosynthetic organic film enriched material's; selecting elastic filler or plastic enriched material; soaking for 1-3 days with 0.1 M hydrochloric acid; drying; fixing a polyvinyl chloride pipe and an aeration device under a device of photosynthetic organic film and elastic filler; culturing; placing the device into an eutrophic water body at 25-35 degrees C; culturing the film for 12 hours; aerating at 3 times per week for 48-168 hours; and absorbing to obtain an organic phosphorus.    USE - The method is useful for removing organic phosphorus in sewage (claimed).    ADVANTAGE - The method removes the organic phosphorus in sewage with reduced cost and less energy consumption.    DETAILED DESCRIPTION - Removing organic phosphorus in sewage comprises pretreating photosynthetic organic film enriched materials, selecting elastic filler or plastic enriched material and then soaking for 1-3 days with 0.1 M of hydrochloric acid and drying, fixing a polyvinyl chloride pipe and an aeration device in a device of photosynthetic organic film and elastic filler, where the polyvinyl chloride pipe is fed into a plastic foam, culturing, placing the device into an eutrophic water body having an illumination intensity of 6000-12000 lux at 25-35 degrees C, culturing the film for 12 hours; aerating at 3 times per week for 48-168 hours, and absorbing to obtain an organic phosphorus.
NOVELTY - Improving citric acid waste water treatment comprises (a) pumping the waste water and supernatant A into a pre-acidification tank for pre-acidification, (b) pumping the acidified waste water and supernatant B into an anaerobic tank to process anaerobically, and (c) allowing the water to overflow from the anaerobic tank into a sedimentation tank, carrying out sedimentation to obtain supernatant and sludge. The volume ratio of supernatant A and citric acid waste water is 1:8-1:2. volume ratio of supernatant B and acidified waste water is 1:3-4.    USE - The method is useful for improving citric acid waste water pre-acidification (claimed).    ADVANTAGE - The method comprises aerobic treatment of the supernatant, thus increasing the pH of anaerobic influent and increasing the concentration of microorganisms in the pre-acidification tank; reduces the impact on anaerobic system; improves the stability and processing efficiency of the anaerobic system; improves the COD removal rate and biogas production; and reduces the operation cost of the enterprises.
NOVELTY - Siphon pressure filter purifying biogas reaction tank, comprises a first tank body (1), an inlet pipe (2), a first filter layer (3), a sealing ring (4), a cover (5), a connector, a first siphon tube, a second filter layer, a second tank body, a second siphon pipe, an outlet pipe, a third tank body, an air valve and a drainage port. The first tank body is connected with the second tank body via first siphon tube. The second tank body is connected with the third tank body via second siphon tube. The first tank body is set with the inlet pipe. The third tank body is set with the outlet pipe.    USE - Used as a siphon pressure filter purifying biogas reaction tank.    ADVANTAGE - The tank is simple, safe, reliable, clean and convenient to use.    DETAILED DESCRIPTION - Siphon pressure filter purifying biogas reaction tank, comprises first tank body, inlet pipe, first filter layer, sealing ring, cover, connector, first siphon tube, second filter layer, second tank body, second siphon pipe, outlet pipe, third tank body, air valve and drainage port, where the first tank body is connected with the second tank body via first siphon tube. The second tank body is connected with the third tank body via second siphon tube. The first tank body is provided with inlet pipe. The third tank body is provided with the outlet pipe. The first tank body is provided with the first filter layer, and the second tank body is provided with the second filter layer. The bottom edge of the first tank body is provided with the drainage port. The third bottom tank body is provided with the air valve.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the siphon pressure filter purifying biogas reaction tank.    First tank body (1)    Inlet pipe (2)    First filter layer (3)    Sealing ring (4)    Cover (5)
NOVELTY - A composite mineral soil remediation agent comprises 60-75 pts. wt. maifanite, 5-15 pts. wt. zeolite, 20-25 pts. wt. peat, 5-15 pts. wt. pumice, 5-15 pts. wt. bentonite, and 0.5-1 pt. wt. microbial fermentation broth.    USE - Composite mineral soil remediation agent (claimed).    ADVANTAGE - The composite mineral soil remediation agent improves quality of soil by adjusting pH value, absorbing heavy metal, and reducing hardening of soil, and is environmentally-friendly.
NOVELTY - Hydrobromic acid prasugrel acetic acid adduct compound (I), is new. (I) is obtained by reacting prasugrel as an intermediate, hydrobromic acid and acetic acid, or reacting prasugrel hydrobromic acid as an intermediate and acetic acid.    USE - Used as hydrobromic acid prasugrel acetic acid adduct compound.    ADVANTAGE - The method utilizes mixed solvent as solvent, is energy saving, economical and environmentally friendly, has simple steps, results in the product with high purity, and is suitable for industrialization.    DETAILED DESCRIPTION - Hydrobromic acid prasugrel acetic acid adduct compound of formula (I), is new. (I) is obtained by reacting prasugrel as an intermediate, hydrobromic acid and acetic acid, or reacting prasugrel hydrobromic acid as an intermediate and acetic acid. An INDEPENDENT CLAIM is also included for synthesizing (I).
NOVELTY - Preparing biodiesel using composite solid-acid catalyst, comprises (i) mixing biomass raw material and methanol in a reaction container, adding a composite solid-acid catalyst, reacting at room temperature to boiling point temperature of reaction liquid under specific pressure for 10 minutes to 24 hours, and obtaining reaction solution; and (ii) completing reacting, separating the solid-acid catalyst using filtration or centrifugal separation method, pouring the liquid phase into a separating funnel, allowing to stand and layering, taking out upper liquid, distilling and recovering methanol.    USE - The method is useful for preparing biodiesel using composite solid-acid catalyst (claimed).    ADVANTAGE - The method: has mild reaction condition; utilizes the catalyst, which has high catalyst activity and high selectivity, and is easy to separate and recycle; does not pollute the environment; and is suitable for industrialized popularization.
NOVELTY - The utility model claims one adjustable's yield electrolytic water reaction system, comprising a reaction tank, a control box, a control panel and a power supply, said reaction tank comprises a first reaction electrode, a reaction electrode, a second temperature sensor and water level sensor, the temperature sensor is set in the reaction tank, the output temperature signal to said control tank, a water level sensor output level signal to said control box, the control box comprises a micro-controller and power conversion circuit, a microcontroller receiving said temperature signal, the water level signal and control command's control panel, the output reference end's reference voltage to said power conversion circuit, a power conversion circuit according to the reference end voltage of the power supply's power into a first reaction electrode and electrode current's second reaction electrode. This utility model's output adjustable's electrolytic water reaction system, hydrogen and oxygen mixed gas's can generate's taking to realize the purpose of saving energy, but also can reaction condition taking.
NOVELTY - The utility model claims one for mine sensor integrated detection system, comprising a device for measuring 's methane gas's high-concentration methane sensor, low-concentration methane sensor, for measuring the 's gas CO's high CONTENT OF CO concentration sensor, a CO concentration sensor for measuring oxygen content 's air's oxygen sensor, a methane sensor, a high-concentration low-concentration methane sensor, high-concentration sensor, a CO concentration sensor, an oxygen sensor is connected with the signal conversion device, the signal conversion device and the voltage follower, the voltage follower connected with the pulse shaping circuit, the pulse shaping circuit is connected with the controller's said controller is respectively connected with the upper computer and liquid crystal display. The utility model's beneficial effects are as follows: simple structure, small volume, low cost, high density of integration is high.
NOVELTY - Apparatus for producing bio-gas from agricultural wastes and domestic organic wastes by composite, comprises four operation units linked together: (a) a material feed device unit comprising an intake port, a toilet inlet, an intake pipe and a forced loading support tool; (b) an anaerobic fermentation tank unit; (c) unit of discharge port and pressurizing tank comprising a discharge port, a pressurizing tank, a circulation entry and an exhaust pipe; and (d) a waste extract treating device unit comprising a waste extract tank and waste extract dry-treating tank.    USE - The apparatus is useful for producing bio-gas from agricultural wastes and domestic organic wastes by composite (claimed).    DETAILED DESCRIPTION - Apparatus for producing bio-gas from agricultural wastes and domestic organic wastes by composite, operating based on the principle of circulation, designed in the spherical shape, comprises four operation units linked together: (a) a material feed device unit comprising an intake port, a toilet inlet, an intake pipe and a forced loading support tool; (b) an anaerobic fermentation tank unit comprising an anaerobic fermentation chamber, a gas-containing chamber and a forced scum-breaking frame; (c) unit of discharge port and pressurizing tank comprising a discharge port, a pressurizing tank, a circulation entry and an exhaust pipe; and (d) a waste extract treating device unit comprising a waste extract tank and waste extract dry-treating tank.
NOVELTY - The apparatus has a fermenter that ferments to-be-processed objects. The stirring blade stirs to-be-processed object in the fermenter. The blade drive shaft rotationally drives the stirring blade. The warm air is penetrated through blow-out hole formed in the hollow pipe of the blade drive shaft. The warm air is supplied from warm air source into the fermenter.    USE - Eco-friendly apparatus for manufacturing compost from organic refuse in home, school, company and Municipal Corporation.    ADVANTAGE - The warm air required for fermentation can be supplied efficiently. The installation of the compost manufacturing apparatus can be made effectively. The compost manufacturing apparatus can be provided with excellent maintainability and high productivity. The external power of the manufacturing apparatus can be reduced as much as possible.
NOVELTY - The apparatus (10) has an electrical storage unit (22) to conserve electric power. A fan (24) forms gas flow which goes to discharge port (16) from suction opening (12). A gas detection element (19) is provided between suction opening and discharge port, for measuring concentration of gas and transmitting gas concentration signal. A control unit (20) generates output signal while judging whether gas concentration is more than threshold value. An output unit (13) outputs measurement result. The gas detection element, control unit and output unit drive with power of electrical storage unit.    USE - Portable gas detection apparatus for measuring concentration of predetermined gas such as oxygen, hydrogen, carbon monoxide, carbon dioxide, propane, butane, and methane in atmosphere.    ADVANTAGE - Since the portable gas detection apparatus is equipped with the hand dynamo, the secondary battery or capacitor is charged immediately and manually even if secondary battery or capacitor is exhausted. The electric power generation of hand dynamo is performed even in night time or dark room interior. Since the fan forms the flow of gases which goes to discharge port from suction opening, and gas detection element exists between suction opening and discharge port, the change of gas concentration can be measured without time lag.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the portable gas detection apparatus. (Drawing includes non-English language text)    Portable gas detection apparatus (10)    Housing (11)    Gaseous suction opening (12)    Output unit (13)    Gaseous discharge port (16)    Gas detection element (19)    Control unit (20)    Electrical storage unit (22)    Electrical generating mechanism (23)    Electrically-driven fan (24)
NOVELTY - A fermentation process apparatus (100) which has heat exchange function comprises fermenter (10) which accommodates fermentation process target objects, such as foodstuff residue and animal excrement, support frame (50) which supports the fermenter, drive mechanism (40) which drives the fermenter, and heat exchanger (31) in which air-nozzle pipe (21) which supplies air protrude in fermenter is arranged.    USE - A fermentation process apparatus (claimed).    ADVANTAGE - Heat generated in fermenter is efficiently recovered while stirring the fermentation process target object with stirring unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the fermenter of fermentation process apparatus.    Fermenter (10)    Door plate (13)    Air-nozzle pipe (21)    Heat exchanger (31)    Drive mechanism (40)    Support frame (50)    Support legs (52)    V-shaped horizontal arrangement materials (55)    Fermentation process apparatus (100)
NOVELTY - Elephantopus scaber is crushed and ultrasonically extracted. The extract is decolored and the solution is concentrated using a macroporous resin adsorption column. Elution is carried out using 50-90% methanol, and the eluate is concentrated by extraction with ethyl acetate. The extracts were collected, reagents are recycled, and the solution is separated using high-speed countercurrent chromatography with UV detector online monitoring. The fractions are collected and dried under reduced pressure to obtain deoxyelephantopin.    USE - Preparation of deoxyelephantopin (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly preparation of high-purity deoxyelephantopin.    DETAILED DESCRIPTION - Elephantopus scaber is crushed and ultrasonically extracted using 5-10 times 60-90% methanol 2-3 times. The extract is decolored using activated carbon, activated carbon is filtered, and the solution is concentrated using a macroporous resin adsorption column. Elution is carried out using 50-90% methanol in an amount 5-10 times the column volume, and the eluate is concentrated by extraction with ethyl acetate. The extracts were collected, reagents are recycled, and the solution is separated using high-speed countercurrent chromatography with UV detector online monitoring. The fractions are collected and dried under reduced pressure to obtain deoxyelephantopin.
NOVELTY - One kind of organic waste material for making soy by saltless ferment organics in the part's bracket is provided with a speed-reducing motor, upper end of the bracket is provided with a fermentation chamber, the fermentation chamber is set in the middle with a connecting shaft, the lower end's's shaft and transmission shaft is connected with the speed reducing motor is connected with upper end of upper's shaft is provided with a stirring blade, a fermentation cabin's side wall is provided with a temperature measuring device, a fermenting chamber's bottom is provided with a discharging port, the upper end of the fermentation chamber is provided with a fermentation chamber's upper cover, side's bracket is provided with an electric hot oil furnace, upper end's electric heating oil furnace is provided with an oil port, the side wall of the fermentation chamber is hollow's, an electric heating oil furnace upper end and side wall of the fermenting chamber is connected with an oil inlet pipe, and an exhaust valve is provided with a circulation pump, an electric heating oil furnace's upper middle part is connected with the side wall of the fermenting chamber is connected with an oil return pipe, side's fermenting chamber is provided with an electric control box, an electric control box is set up with a temperature display meter, Temperature display meter is connected with the temperature measuring device;
NOVELTY - The utility model claims one for pre-treated straw multifunctional tank, comprising a slurry pool uniformly's cylindrical slurry pool uniformly up close to the outer wall's circumferential surface is provided with stack retting tank, said stack retting tank and homogenizing tank cavity of the said stack retting tank and homogenate tank is provided with a lifting plate, stack retting tank is provided with a transparent cover plate. The utility model combines the stack retting tank and slurry pool uniformly building a building as a whole, which can ensure the straw rotten's waste water generated in the process , which causes resource waste and pollution. Meanwhile, it can according to straw rotten's time to rationally setting the stack retting tank, convenient management, reduces the manual cost and management cost, it's high practicability.
NOVELTY - The utility model claims upper one of compost tea fermentation device, mainly comprising a tank body (1), a liquid circulating pump (4), an air compressor (5), a liquid filter (6), a liquid filter screen (15), tea bag frame (16) and a tea bag (17), the tank body (1) is provided with an upper circulating water pipe (7) and the water level display (8), a tank body (1) is provided with a vent pipe (14) is provided with a through water drain valve's outer bottom tank body (13), a tank body (1) in the middle is provided with a filter screen (15), a filter screen (15) is equipped with a tea bag (16). This utility model is one kind of directly used for production facility's water fertilizer integrated new compost tea fermentation device, time saving and labour saving by's.
NOVELTY - The utility model claims upper one static aerobic composting reactor device, multiple layers of high temperature resistant polyvinyl chloride pipe (4) and ecological bag's charge (2) is paved on the non-woven fabrics filtering pad (8), ecological bags (2) in the length direction and ecological bag's length direction is vertical to the adjacent layers, each layer of high temperature resistant polyvinyl chloride pipe (4) and the adjacent layer's high temperature resistant polyvinyl chloride pipe (4) are vertical to each other, the upper layer's ecological bags (2) is set dropping head (1), and pipe (3) is connected with the oxygen increasing diving pump (7) is connected with the oxygen increasing diving pump (7) through pipe (3) is connected to the liquid tank (10). Using conventional agricultural machinery as assistant, straw raw material and auxiliary material local materials, ecological bag, heat-insulating non-woven fabric AND TPU waterproof ventilating film's new material, it can realize high quality compost fermentation, fermenting the finished product and storing high nutrient content, simple and convenient use.
NOVELTY - Active organic biological fertilizer is produced by adding 50-80% dry soy sauce residue and other raw materials, then adding water and composite microbial agent, stacking to a height of 1-3 m, and fermenting at controlled oxygen supply.    USE - Method of producing active organic biological fertilizer (claimed) used for promoting crop growth.    ADVANTAGE - The method can realize waste resource utilization by using soy sauce residue which is rich in protein and involves microbial decomposition to generate a large amount of active substance such as vitamin, amino acid, humic acid, sodium humate and potassium humate and other biochemical metabolite.
NOVELTY - A 2,3,4,4'-tetrahydroxybenzophenone is prepared by mixing gallic acid and p-hydroxybenzoic acid with 1:1-5 mole ratio, adding hydrocarbon reagent with 3-5 times higher boiling point, mixing at 100 revolutions/minute speed, slowly adding boron trifluoride etherate with 2-4:1 volume ratio, heating in oil bath at 100-120 degrees C for, mixing at 100 revolutions/minute speed for 1-6 hours, cooling to room temperature, precipitating, collecting yellow precipitates, adding water and sodium bicarbonate, centrifuging, crystallizing, washing with distilled water, and drying at 40-60 degrees C.    USE - Method for preparing 2,3,4,4'-tetrahydroxybenzophenone (claimed).    ADVANTAGE - The method has low cost, high yield, simple operation, low toxicity, and short reaction time.
NOVELTY - A benzothiazole heterocyclic compound is synthesized by performing direct oxidation condensation cyclization reaction of alcohol and o-aminothiophenol in presence of water-soluble catalyst and air as oxidant in which water-soluble catalyst is inorganic alkali, reaction temperature is 60-160 degrees C, and reaction time is 1-48 hours.    USE - Synthesis of benzothiazole heterocyclic compound (claimed).    ADVANTAGE - Synthesis process is environment-friendly and easy to operate, has simple and mild reaction condition and high recovery rate, and does not need inert gas, raw material is stable and has low toxicity, and catalyst has good water solubility.    DETAILED DESCRIPTION - A benzothiazole heterocyclic compound of formula (III) is synthesized by performing direct oxidation condensation cyclization reaction of alcohol compound of formula (I) and o-aminothiophenol compound of formula (II) in presence of water-soluble catalyst and air as oxidant in which water-soluble catalyst is inorganic alkali, reaction temperature is 60-160 degrees C, and reaction time is 1-48 hours.    R1=Ph, substituted aryl, or substituted heteroaryl or alkyl; and    R2=alkyl, alkoxy, halo, NO2, aryl, or heteroaryl.
NOVELTY - Strontium ranelate is synthesized by dissolving 5-amino-4-cyano-3-(2-methyl/ethoxy-2-oxoethyl)-2-thiophene formate/ethyl and catalyst in solvent, adding potassium carbonate, dropwise adding alkylating agent, refluxing for 2-5 hours, to obtain crystallized orange-yellow ranelate tetramethylammonium/ethyl, dissolving in mixed solvent e.g. 15-55% aqueous methanol, adding ammonia, reacting at room temperature, vacuum distilling to remove organic solvent, adding strontium chloride, heating to 40-80 degrees C, reacting for 5-8 hours, filtering while hot, and washing filter cake with hot water.    USE - Synthesis of strontium ranelate for traditional Chinese anti-osteoporosis drug (claimed).    ADVANTAGE - The synthesis of strontium ranelate is cheap, non-toxic, environment-friendly, suitable for industrialized production, simplifies refining process, and improves product purity.    DETAILED DESCRIPTION - Strontium ranelate of formula (I) is synthesized by dissolving 5-amino-4-cyano-3-(2-methyl/ethoxy-2-oxoethyl)-2-thiophene formate/ethyl of formula (III) and catalyst in solvent, adding potassium carbonate, dropwise adding alkylating agent, refluxing for 2-5 hours, to obtain crystallized orange-yellow ranelate tetramethylammonium/ethyl of formula (II), dissolving in mixed solvent which is 15-55% aqueous methanol or ethanol, adding ammonia, reacting at room temperature, vacuum distilling to remove organic solvent, adding strontium chloride, heating to 40-80 degrees C, reacting for 5-8 hours, filtering while hot, and washing filter cake with hot water.
NOVELTY - Refined oil is prepared by filtering pressed or extracted non-edible animal and plant crude oil to remove solid particulate, heating to 40-80 degrees C, adding 1-3% conversion-complexing agent while stirring at 100-1000 rpm, stirring at constant temperature for 50-90 minutes, centrifuging to obtain degummed oil, dehydrating degummed oil at 95-105 degrees C with vacuum degree of 0.07-0.08 MPa for 15-25 minutes to remove trace water, heating to 90-110 degrees C while stirring, adding 1-4% sorbent, stirring at constant temperature for 10-30 minutes, and filtering.    USE - Preparation of refined oil for preparing biological jet fuel and biodiesel (all claimed).    ADVANTAGE - Refined oil has low impurity content, and preparation reduces loss, energy consumption, production cost, improves refining yield, has no wastewater discharge, high refining efficiency and stability and simplifies refining process.
NOVELTY - A hydrogen generator comprises hydrogen generating device with controller, rectification circuit, three-phase or single-phase alternating current power supply, direct current switch circuit, intelligent program control unit input end, circulating cooling water tank (2), closed loop feedback control, electrolysis groove (8), cooling system, heat exchanger (7), oxygen and hydrogen outlet (4), through hole (21), and display or alarm.    USE - Hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen generator.    Water tank (2)    Oxygen and hydrogen outlet (4)    Heat exchanger (7)    Electrolysis groove (8)    Through hole (21)
NOVELTY - The system (1) has a carbonization apparatus (3) which heats the to-be-processed object (W). Heat recovery equipment (4) recovers heat from the carbonization waste gas (CG) emitted from carbonization apparatus. Heat recovery equipment reuses the recovered heat as heat source of drying machine (2). A preset path transfers the incineration waste gas (BG) from an incinerator (5) to heat recovery equipment and transfers carbonization waste gas to heat recovery equipment, so that combined carbonization waste gas and incineration waste gas is sent into heat recovery equipment.    USE - Dry carbonization system for carbonizing sewage-sludge coconut urine sludge for manufacturing fuel and fertilizer.    ADVANTAGE - The preset path transfers the incineration waste gas from an incinerator to heat recovery equipment and transfers carbonization waste gas to heat recovery equipment, so that combined carbonization waste gas and incineration waste gas is sent into heat recovery equipment, even when carbonization exhaust gas amount of carbonization apparatus is fluctuated by the use of the carbonized material. The total exhaust gas amount sent into the heat recovery equipment can be maintained constantly. The stable heat recovery process can be attained. The total exhaust gas amount sent into the heat recovery equipment can be stabilized. The fuel-efficient operation can be performed.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the dry carbonization system. (Drawing includes non-English language text)    Dry carbonization system (1)    Drying machine (2)    Carbonization apparatus (3)    Heat recovery equipment (4)    Incinerator (5)    Incineration waste gas (BG)    Carbonization waste gas (CG)    To-be-processed object (W)
NOVELTY - A glucoamylase variant comprising amino acid substitutions corresponding to positions: 50, 417, 430, 511, 539, and 563 of SEQ ID NO. 2, or corresponding positions in a parent glucoamylase, where the glucoamylase variant has at least 90% sequence identity with SEQ ID NO. 2, and where the amino acid substitution at position 50 is Met50Tyr, Gly, Phe, or Lys, is new.    USE - The glucoamylase variant and enzyme composition are useful for processing starch to produce a composition comprising glucose, and for fermenting the composition to an end product selected from alcohol (i.e. ethanol), citric acid, lactic acid, succinic acid, monosodium glutamate, gluconic acid, sodium gluconate, calcium gluconate, potassium gluconate, glucono delta-lactone, sodium erythorbate, omega 3 fatty acid, butanol, lysine, itaconic acid, 1,3-propanediol, biodiesel, or isoprene (all claimed).    ADVANTAGE - The new glucoamylase variant exhibits more desirable properties such as improved thermostability, improved specific activity, and/or resistant to oxidation-related activity loss.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an enzyme composition comprising the glucoamylase variant above; and    (2) a method of processing starch by contacting a starch substrate with the glucoamylase variant above to produce a composition comprising glucose.
NOVELTY - Preparing a fuel composition comprises (a) reducing, by cryogrinding, a biomass product to obtain a powder, and (b) mixing the powder with at least one liquid fuel.    USE - The method is useful for preparing a fuel composition (claimed).    ADVANTAGE - The method ensures simple, economic and safe preparation of the fuel composition from biomass product, reduces the biomass product into a very fine powder without altering its content during the production of fuel composition, and allows good preservation of the chemical compounds within the biomass product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel composition obtained by the method comprising a powder of the cryogenically ground biomass product and a liquid fuel.
NOVELTY - Cellulose biomass feedstock is solubilized by biomass modification process which modifies lignin contained in the biomass feedstock containing a cellulose by pullling apart from the cellulose, solubilization process which heats the modified biomass feedstock in an atmosphere below saturation water vapor pressure to convert into a water soluble mixture, and extraction process which separates residue in the solubilized mixture from solubilization liquid which contains water and lignin.    USE - A solubilizing method of cellulose biomass feedstock (claimed) for manufacture of biomass fuel.    ADVANTAGE - The processing steps are reduced, production time is short, and manufacturing cost is cheap.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the solubilizing method of cellulose biomass. (Drawing includes non-English language text).
NOVELTY - The ammonia plant system has two stage suction air chillers (250) which are provided in an air compression system that chills incoming air by heat exchange with expanded high pressure ammonia from the ammonia compression system of the ammonia plant. The additional two stage air chillers (230,235,240) are provided between each of the air compressors of the air compression train (200). Each air chiller is provided for chilling incoming air by heat exchange with expanded high pressure ammonia from the ammonia compression system of the ammonia plant.    USE - Ammonia plant system for upgrade utilizing direct multistage chilling system in ammonia plant air compression train.    ADVANTAGE - By integrating refrigerant ammonia stream at different temperature levels from existing or new ammonia compression system, the air chilling can be lead to significant increase in process air compression capacity and higher energy efficiency in efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an ammonia plant upgrade method for utilizing an indirect multistage chilling system in the ammonia plant air compression train.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the direct integrated multistage air chiller.    Air compression train (200)    Additional two stage air chillers (230,235,240)    Air chiller (250)    Ammonia compression train (300)    Compressor casing (310)
NOVELTY - Solid fuel in the form of pellets comprises residues of fruit or berries (peel, pulp, endocarp, stones) and organic adhesive, and less than 15%, preferably less than 10% of water. The solid fuel is in spherical shape, and comprises more than 40 wt.% of ground endocarps having a particle size of 3-9 mm.    USE - The solid fuel is useful for feeding heating modules (claimed) such as chimneys, fireplaces and boilers.    ADVANTAGE - The solid fuel is cost-effective, and has high calorific value.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the solid fuel, comprising grinding the residues and/or endocarps, then mixing with the starch or flour in form of aqueous bone paste, shaping, and drying; and    (2) a system for feeding heating modules, comprising a feed pipe or conduit of the fuel, and a unit for introduction of the fuel in the form of beads coupled to a cylinder pusher motor receiving the fuel through lateral openings driving the fuel to a funnel connected to an axial pipe, where the feed pipe has an interior diameter slightly greater than a diameter of the fuel to be transported.
NOVELTY - Fuel additive composition of at least four components comprises: 0.5-85% of degummed lipid acids or lipid esters; 0.5-85% of castor oil; 0.5-85% of pour point depressant; and 0.5-85% of glycerol monooleate or glycerol monostearate.    USE - The fuel additive composition is useful for running a diesel engine during winter time (claimed).    ADVANTAGE - The fuel additive composition: is added as an additive to gasoline resulting in improved fuel economy when compared to the gasoline used alone; can be added to any fuel and results in an increased shelf life; is safer for the environment; can be used after-market fuel additive; meets or exceeds minimum requirements for finished fuels while offering the benefit of single application of a non-hazardous additive and can replace several additives currently in use at less cost to the fuel product; and is environmentally-responsible and contains no metals or sulfur.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method of using a fuel additive comprising running a diesel engine during winter time on diesel fuel mixed with the additive composition;    (2) a composition comprising the fuel additive composition and jet fuel;    (3) a composition comprising the fuel additive and a fuel comprising diesel, biodiesel, gasoline, or jet fuel; and    (4) preparing a fuel additive, comprising, in the following sequence, placing 0.5-85% of degummed lipid acids or lipid esters in a vessel and heating to 84-100 degrees F, adding 0.5-85% of castor oil and heating to 84-100 degrees F, adding 0.5-85% of pour point depressant and heating to 84-100 degrees F and adding 0.5-85% of glycerol monooleate or glycerol monostearate and blending the mixture at 84-100 degrees F for 20 minutes with mild agitation.
NOVELTY - Producing a compost comprises contacting shells from one or more shellfish with fruit to form a mixture, maintaining the mixture for a time sufficient to form compost. The compost is formed in less than eight weeks.    USE - The method is useful for producing a compost, which is useful for producing a product including calcium salt, chitosan and/or chitin (all claimed) where the calcium salt is calcium acetate.    ADVANTAGE - The method simply and rapidly produces the odorless compost with high efficiency in a convenient and eco-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method-1 for producing a product comprising composing shells from the shellfish with fruit until a product is formed; and    (2) reducing odor associated with shell waste from shellfish comprising contacting the shell waste with a fruit product.
NOVELTY - Photobioreactor (1) comprises a transparent conduit system for the flow of the culture suspension, preferably algae substrate. The transparent conduit system is stack-shaped.    USE - The photobioreactor is useful for cultivating phototrophic organism, preferably algae (claimed).    ADVANTAGE - The photobioreactor: has roof with good light transmittance; and provides improved airflow with reduced energy expenditure, thus it allows easy flow of the culture suspension.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) an arrangement of a light-permeable support element (6) for a photobioreactor for cultivating phototrophic organism, in which the support element is held in the wall region of the outer shell of the photobioreactor, and the support element is designed to be closed in the horizontal extension and has a truss structure; and    (2) a biogas plant for producing biogas comprising a photobioreactor and a fermenter (11) which is arranged inside the photobioreactor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a photobioreactor and a biogas plant.    Photobioreactor (1)    Wall region (2)    Translucent roof (3)    Support element (6)    Fermenter (11)
NOVELTY - Device for heating of biofuels, comprises a case made with heat-insulating layer, input and output connecting pipe, ultrasonic transducer, installed inside the case is a heater, where inside the case of heater is installed SHF-heater, where the case of heater is made from copper.    USE - The device is useful for heating of biofuels (claimed).
NOVELTY - Preservation method of distillation remaining slurry involves performing saccharification of substrate comprising biomass with saccharogenic amylase in 1st reaction tank, accommodating the saccharification solution and biomass residue in 2nd reaction tank, performing fermentation using saccharification solution and fermented microbe to obtain fermentation solution, collecting and preserving the distillation remaining slurry remained after distillation of fermentation solution and adding calcium cyanamide to distillation remaining slurry.    USE - The method is useful for preserving distillation remaining slurry (claimed).    ADVANTAGE - The method enables to preserve distillation remaining slurry for long period of time.    DETAILED DESCRIPTION - Preservation method of distillation remaining slurry involves performing saccharification process of substrate comprising biomass with saccharogenic amylase in 1st reaction tank, and obtaining saccharification solution and biomass residue, accommodating the saccharification solution and biomass residue in 2nd reaction tank, performing fermentation using saccharification solution and fermented microbe to obtain fermentation solution, collecting and preserving the distillation remaining slurry remained after distillation of fermentation solution when manufacturing bioethanol according to the process of distilling the fermentation solution and obtaining ethanol, and adding calcium cyanamide to distillation remaining slurry, where the concentration of the nitrogen in the calcium cyanamide is 0.08-0.8 %mass.
NOVELTY - The present disclosure relates to a solid catalyst for the production of biodiesel. The solid catalyst in the present disclosure works efficiently on a variety of feed stocks under ambient conditions and achieves complete transesterification at a very high conversion rate. The present disclosure also relates to a process for the preparation of the solid catalyst. The present disclosure further relates to a process for the production of biodiesel from various feedstocks by using the solid catalyst.
NOVELTY - An anaerobic-treatment installation (S1) produces methane gas (X5) by carrying out anaerobic treatment of waste water containing organic substance in a methane fermentation tank (3). When supply of the waste water to the methane fermentation tank from upstream installation which discharges the waste water is stopped, the methane fermentation tank is cooled and activity of a methane producer is reduced.    USE - Installation is used for anaerobic-treatment method (all claimed) used in kraft pulp production.    ADVANTAGE - The anaerobic-treatment installation stably provides methane gas and maintains activity of methane producer in high state, with reduced content of inhibitor which does not melt into waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of anaerobic-treatment installation. (Drawing includes non-English language text)    Methane fermentation tank (3)    Anaerobic-treatment installation (S1)    Evaporator drain water (X1)    Methane gas (X5)    Magnesium hydroxide (X6)
NOVELTY - A plant nutrient composition comprises liquid fraction which is obtained by separating into solid and liquid the methane fermentation waste water which methane-fermented used-coffee-powder containing process liquid, or liquid fraction processed material.    USE - Plant nutrient composition for purifying arabinogalactan protein (claimed).    ADVANTAGE - The used coffee powder is used effectively and recovered as biogas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of plant nutrient composition which involves performing methane fermentation process of used-coffee-powder containing process liquid, and solid-liquid-separation process of separating into solid and liquid the methane fermentation waste water obtained at methane fermentation process obtaining liquid fraction; and    (2) purification of arabinogalactan protein which involves isolating arabinogalactan protein from plant nutrient composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing process of plant nutrient composition.    Solubilization tank (1)    Methane fermentation tank (2)    Centrifugation part (3)    Mixing tank (10)    Heater (11)    PH control part (12, 40)    Processing tank (20)    Centrifugal separator (30)
NOVELTY - A substrate formed using biomass is fermented using microbe, and subjected to saccharification process using saccharogenic amylase in a reactor. A component-containing solid material is separated from the fermentation processed material, to obtain fermentation solution. The fermentation solution is distilled for manufacturing bioethanol, and distillation residual liquor is obtained. Calcium cyanamide is added to the distillation residual liquor such that nitrogen concentration is 0.08-0.8 %mass, to preserve distillation residual liquor.    USE - Preservation of distillation residual liquor (claimed).    ADVANTAGE - The method enables preservation of distillation residual liquor efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacture of bioethanol. (Drawing includes non-English language text)
NOVELTY - Obtaining hydrogen via supplying substances in water medium containing metal into a reactor, where the substance containing metal is insulate from the walls of reactor and is supplied to it high-voltage potential from a transformer of Tesla with a voltage of 1-100 kV with a frequency of 1-100 kHz and microplasma discharges in water are removed from the surface of the substances containing metal oxide film activating a reaction of aqueous oxidation of metals.    USE - The method is useful for obtaining hydrogen (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for obtaining hydrogen from water, comprising reactor with the metal-containing substance with water medium with branch pipe for the input of water, withdrawal of hydrogen and products of reaction of oxidation of substances metallic, where the substance containing metal is placed into a container, electric insulated from the walls of reactor, and is connected through the feedthrough insulator with high-voltage high-frequency resonance transformer of Tesla, with an electrical power source with a voltage on high-voltage outlet of transformer 1-100 kV and a frequency of 1-100 kHz.
NOVELTY - A bismuth subsalicylate is prepared by mixing bismuth hydroxide powder and pure water according to liquid-solid ratio, stirring to obtain uniform suspension, adding salicylic acid, heating, reacting under maintained temperature, keeping in dark, filtering, washing using boiling water, drying, crushing, sieving, and storing.    USE - Preparation of bismuth subsalicylate (claimed).    ADVANTAGE - Process has reduced generation of wastewater and mist, reduced sewage treatment cost, reduced production cost, and improved product yield and quality, and is safe.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparing bismuth subsalicylate. (Drawing includes non-English language text).
NOVELTY - A benzyl nicotinic acid onium salt is synthesized by completely dissolving sodium hydroxide in water, adding nicotinic acid at 40-60 degrees C, completely dissolving by stirring, adding composite catalyst and buffering agent, dropwise adding benzyl chloride, and reacting for 1-2 hours at 70-100 degrees C in which composite catalyst is mixture of potassium carbonate (K2CO3) or sodium carbonate (Na2CO3), and quat.-ammonium salt i.e. tetrabutylammonium bromide, benzyl triethyl ammonium chloride, dodecyl trimethyl ammonium chloride, and/or trioctyl methyl ammonium chloride.    USE - Synthesis of benzyl nicotinic acid onium salt for alkaline non-cyanide zinc plating solution additive used for plating cast iron and high carbon steel.    ADVANTAGE - Synthesis method is low in cost and environment-friendly, and has high yield, short reaction time, and high product purity, and plating solution has deep plating ability.    DETAILED DESCRIPTION - A benzyl nicotinic acid onium salt is synthesized by completely dissolving sodium hydroxide in water, adding nicotinic acid at 40-60 degrees C, completely dissolving by stirring, adding composite catalyst and buffering agent, dropwise adding benzyl chloride, and reacting for 1-2 hours at 70-100 degrees C in which composite catalyst is mixture of potassium carbonate (K2CO3) or sodium carbonate (Na2CO3), and quat.-ammonium salt i.e. tetrabutylammonium bromide, benzyl triethyl ammonium chloride, dodecyl trimethyl ammonium chloride, trioctyl methyl ammonium chloride, hexadecyl trimethyl ammonium bromide, and/or benzalkonium bromide, and buffering agent is sodium bicarbonate, sodium carbonate, sodium acetate, or boric acid.    DESCRIPTION OF DRAWING(S) - The drawing shows an HPLC chromatogram of a benzyl nicotinic acid onium salt liquid.
NOVELTY - A B5 comprises 30-50 pts. wt. rubber seed oil biodiesel, 10-20 pts. wt. bramble seal oil biodiesel, and 20-30 pts. wt. waste oil biodiesel.    USE - B5 used for biodiesel oil (claimed).    ADVANTAGE - The B5 has readily available raw materials and high oil content of non-food raw materials, and provides superior performance with biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of B5 comprising stirring and uniformly mixing raw materials, pressurizing at 2-3 atmospheric pressure, and filling with 0.5 nm size absorption resin into first-stage adsorption column and 0.8 nm adsorption resin into second-stage adsorption column.
NOVELTY - This utility new type household waste wood and waste paper disposing and reusing device, wherein it is composed of switch (1), a temperature control module (2), a shell (3), a feeding port (4), a smoke (5), a transparent cover (6), a drain pipe (7), a heating disc (8) and a carbonization chamber (9), the left side of the shell is equipped with a switch, the switch is connected with the temperature control module, an internal shell is a carbonization chamber, a carbonization chamber is equipped with heating plate, shell right side is equipped with a transparent plastic shell right side is connected with smoke evacuation is connected with right side shell is connected with drain-pipe, a transparent cover is high temperature resistant engineering plastic, heat-resistance temperature can reach 700 degrees C, the household waste wood and waste paper processing device, a power supply voltage of 220V, which is suitable for home use, the waste wood and waste paper can be converted into organic fertilizer, using the home, it is a kind of protecting environment and saving energy.
NOVELTY - The invention discloses to cetane and lubricity improvers, particularly the invention relates to fuel composition comprising (a) at least 99 wt% of a base fuel, and (b) cetane improvers selected fiom fatty amide or fatty alcohol nitrate ester in the concentration range of 0.02 to 0.2 wt%. The invention also relates to improved process for the preparation of cetane and lubricity improvers. More particularly the invention relates to cetane and lubricity improvers derived from natural, renewable triglycerides, esters and alcohols thereof and are environment friendly.
NOVELTY - Integrated treatment and utilization method of pig manure, involves (a) washing pig urine in water, and discharging the resultant liquid into fermentation digester (biogas), (b) collecting pig manure, dehydrating the pig manure, subjecting the manure to solid-liquid separation and introducing the liquid into digester, and (c) drying the solid pig manure and mixing the dried manure with rapeseed to obtain organic fertilizer, fermenting the solid manure (feed for fish and maggots), and applying the obtained manure as organic fertilizer to field.    USE - Integrated treatment and utilization method of pig manure (claimed) which is useful as organic fertilizer.
NOVELTY - Processing triethylamine using a membrane separation method comprises taking glycine circulating mother liquid and methanol, selecting nanofiltration membrane having a molecular weight of 80-300 Daltons and a pressure of 1.5-4 Mpa at 20-40 degrees C, mixing using a film apparatus to obtain a raw material product, distilling, recycling the product, adding water in the product, rectifying and recovering methanol, adding calcium oxide, drying, adding concentrated sulfuric acid to obtain a calcium sulfate sediment, filtering the calcium sulfate liquid, and drying.    USE - The method is useful for processing triethylamine (claimed).
NOVELTY - Palladium-based catalyst comprises an alumina carrier and a loading component. The loading component is divided into two active components (in wt.%): a primary main active component is palladium (0.0l-0.08) and a co-active components are iron, nickel and lanthanum (0.001-3) of total weight of catalyst.    USE - Palladium-based catalyst for performing selective hydrogenation (claimed) for producing butadiene and acetylene.    ADVANTAGE - The catalyst composition is prepared in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing catalyst composition, which involves:    (A) loading simultaneously primary main active component and co-active component on alumina carrier; and    (B) loading first co-active component on an alumina carrier and then the primary main active components.
NOVELTY - The method involves collecting the household garbage and separating the collected garbage into organic matter and inorganic matter. The separated garbage is passed inside organic and inorganic pit tanks (1,2). The garbage accommodated inside the pit tank is dried and dehydrated. The garbage is crushed using the crushing rollers. The crushing rollers are arranged at specific distance from each other. The garbage is filtered by using mechanical filter screen. The sewage is cleaned and refined. The processed sewage is passed through outlet of inorganic garbage pit tank.    USE - Method for recycling and processing household garbage sewage such as domestic waste water.    ADVANTAGE - The household garbage sewage can be processed easily and effectively without causing environmental pollution. The burning of garbage stored in the pit tank is prevented, such that the environmental pollution can be prevented effectively. The domestic garbage can be separated into organic and inorganic substances.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the sewage processing method. (Drawing includes non-English language text)    Pit tanks (1,2)
NOVELTY - A soil conditioner comprises Azotobacter, phosphorus bacteria, potassium bacteria, Bacillus, Pythium, fulvic acid, an organic fertilizer, and trace element.    USE - A soil conditioner.    ADVANTAGE - The soil conditioner improves soil fertility and chemical physical fertility, and achieves high crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the soil conditioner, comprising uniformly mixing Azotobacter, phosphorus bacteria, potassium bacteria, Bacillus, and Pythium, where each kind of bacteria effective viable bacteria number is more than 1x 1010; uniformly mixing fulvic acid, organic fertilizer, ferrous sulfate, magnesium sulfate, manganese sulfate, zinc sulfate, and copper sulfate, and sterilizing at high temperature; uniformly mixing the mixtures together, and stirring uniformly, and fermenting at 25-30 degrees C at aerobic atmosphere conditions for 24-48 hours; and low-temperature drying at 40 degrees C to obtain a moisture content of 18-30%.
NOVELTY - Synthesis and purification of mefenamic acid, involves the following steps: adding 2-chloro-benzoic acid, acid binding agent, N,N-dimethyl formamide and sodium carbonate in proper proportion and stirring; adding 2,3-dimethylaniline in proper proportion, at certain temperature in the presence of a catalyst for condensation reaction to obtain mefenamic acid crude product; decoloring the mefenamic acid crude product in an organic solvent; crystallizing; and refining to obtain the mefenamic acid finished product.    USE - For synthesis and purification of mefenamic acid (claimed) useful as non-steroidal anti-inflammatory drug.    ADVANTAGE - The process compared with the traditional technique, provides high target product yield; is simple; has mild reaction condition; and is suitable for industrial production. The purification process is simple. The product obtained has high purity The main solvent N,N-dimethyl formamide can be recycled, thus further reduces the production cost.
NOVELTY - The utility model claims one by multi-energy for preparing hydrogen and supplying green energy's system, comprises a renewable energy generating device, a water electrolysis device, hydrogen compression device, hydrogen storing device, a power distribution device, a hydrogen fuel cell, a hydrogen furnace, hydrogen leakage detecting device, a fresh water storage device, a water processing device, a renewable energy source generating device and the power distribution device is connected with the power distribution device is respectively connected with the water electrolysis device, device for obtaining renewable energy source's power distribution electric energy input power distribution device's water electrolysis device, electric device, hydrogen fuel battery through power distribution device are respectively distributed to the water electrolysis device, electric device, hydrogen storing device and a hydrogen furnace, the hydrogen furnace supplying fuel, hydrogen leakage detection device is used for detecting the hydrogen storage device Whether there is leakage of hydrogen hydrogen furnace, hydrogen fuel battery and hydrogen's produced by fresh water storage device, a water processing device for storage and taking.
NOVELTY - An energy-saving one methanol synthesis system, comprising the steps of synthesizing tower, a steam drum, a steam over-heater, boiler water feeding pump, the inlet and outlet heat exchanger, air cooler, the water cooler, an adsorption tower, high pressure methanol separator, a flash tank, a circulating machine and fuel gas power generation set, said absorption tower and said inlet and outlet heat exchanger is connected with the said synthesizing tower inlet and outlet heat exchanger is connected with the boiler water supply pump is connected with the said synthesizing tower is connected with said high pressure methanol separation tower and the water cooler is connected with said flash tank and the high pressure methanol separation tower is connected with said steam and synthesis tower is connected with said circulation motor and the high pressure methanol separator, the inlet and outlet heat exchanger is connected with the steam over-heater and the steam drum, said flash tank is connected with the said air inlet and outlet heat exchanger is connected with the said water cooler and the air cooler; The utility model can product 1.0MPa steam and 2.5MPa steam, and cooling and water cooling to replace the traditional's water-cooling process, and it has high efficiency, it's energy-saving.
NOVELTY - This utility model belongs to one kind of environment-friendly crop straw carbon and tar, wood wax liquid recycling system, comprising a conveyor (1) and a draught fan (7), wherein the conveyor system's (1) and the dust remover (3) is set between the furnace (2), the dust remover (3) is connected with the gas-liquid separator (5) is equipped with tar separator (4), the gas-liquid separator (5) is connected with the draught fan (7) is set between the wax liquid separator (6). Carbonizing furnace (2) the inner wall of the shell's patched refractory brick (2-4), air duct (2-7) is set in the middle, the lower part is cooling layer (2-8), a tar separator (4) upper part are mounted a plurality of double-pipe beam (4-3), and the lower end body is provided with a tar recycling layer (4-2). The utility model claims the straw into carbon, saves the energy's, recycling the tar and wood wax liquid useful material, low labour intensity, good for environmental protection, has no pollution, the product quality is stable, the production efficiency is high.
NOVELTY - This utility model claims one kind of alcohol-based liquid fuel production system, comprising a raw material tank, a filter, an additive tank, tank, air compressor, air compressor, a finished product tank and so on, wherein said raw material tank through the filter's and synthesizing tank is connected with the additive tank through the filter and synthesizing tank is connected with the air compressor by the air compressor with synthesizing tank, synthetic tank through the filter and a finished product tank. This utility model uses industrial methanol as raw material, and then adding the additive mixing and stirring, the product quality reaches the national standard for alcohol base fuel, the product can be replaced natural gas for family, but also can replace liquefied petroleum gas, diesel fuel in hotel, hotel, school dining hall and so on.
NOVELTY - The utility model claims one integrated biological diesel oil preparation device, comprising a box body and a box body's in the the preparation of biologic diesel fuel, the preparation of biologic diesel fuel gasifying device esterification reaction kettle, ester exchange reaction, neutralizing water washing tank and a drying device, wherein the gasifying esterification reaction kettle, ester exchange reaction, neutralizing water washing tank and a drying device are connected in turn through pipeline, up pipeline is provided with a conveying pump. The utility model can generally's vehicle taking transport, can be adapted to different sizes of city waste oil to generate different's processing device. In addition, the utility model technical process for preparing biodiesel's, in the under normal temperature and normal pressure state, it does not need high pressure container and distillation column's traditional process, and it has high safety factor, Jian-an is simple and convenient, the operation cost is low, the technique flow is short and so on.
NOVELTY - One of hydrogen and oxygen generator, this utility model relates to one kind of hydrogen and oxygen generator, this utility model in order to solve the problem in the existing technology's between hydrogen and oxygen generator pole piece's distance, low energy consumption, high cost, low working efficiency's, said hydrogen and oxygen generator comprises a cathode end plate, an anode end plate, an electrolyte circulating pump population tube, electrolyte circulating pump outlet pipe, an aeration pipe, an electrolyte circulating pump, a liquid level observing pipe, the pole piece assembly and connecting piece; the pole piece assembly are set side by side, one end component's is provided with a cathode end plate, the other end plate assembly are respectively provided with one's liquid level observation pipe upper is provided with a male end plate, cathode end plate and anode end plate, one end of the upper end plate is provided with an aeration pipe, an electrolyte circulating pump tube's population through cathode end plate and pole piece component is set on the anode end plate upper, electrolyte circulating pump outlet pipe's one end passes through the cathode end plate and pole piece component is set on the anode end plate up; The utility model is used in the hydrogen-oxygen mixed gas producing field.
NOVELTY - Methane gas-rich reactor system comprises reactor (100), synthesis gas inlet (101), product gas outlet (102), reaction-absorption area (105) comprising methanation catalyst and adsorbent capable of adsorbing and/or absorbing carbon dioxide and/or sulfide; adsorbent regenerator (200), waste adsorbent conveying pipeline, feed pipe channel, and a regenerated sorbent conveying pipeline.    USE - Methane gas-rich reactor system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method using the reactor system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of methane gas-rich reactor system.    Reactor (100)    Synthesis gas inlet (101)    Product gas outlet (102)    Reaction-absorption area (105)    Adsorbent regenerator (200)
NOVELTY - A gas hydrate reactor comprises heat preservation jacket (1), piston (7), micropore reactor (4), hydraulic system (26, 27), rod (29, 31), and connecting rod (8, 9).    USE - Gas hydrate reactor.    ADVANTAGE - The reactor solves hydrate slurry in liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for three-phase separation comprising processing reaction gas and solution using the reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of gas hydrate reactor.    Heat preservation jacket (1)    Micropore reactor (4)    Piston (7)    Connecting rod (8, 9)    Hydraulic system (26, 27)    Rod (29, 31)
NOVELTY - Preparation of carbon-coated titanium carbide loaded with nickel and cobalt tetroxide material comprises taking titanium alloy sheet, introducing hydrogen and nitrogen, heating, introducing acetone and cooling; taking carbon-coated titanium carbide nanowire array as working electrode, platinum electrode as counter electrode, saturated calomel electrode as reference electrode, cobalt nitrate and triethanolamine as electrolyte, electrodepositing; soaking in ethanol and water, carrying out in-situ growth with oxalic acid; and drying.    USE - Method for preparing carbon-coated titanium carbide loaded with nickel and cobalt tetroxide material used for hydrogen peroxide catalytic electrochemical reduction (claimed).    ADVANTAGE - The method ensures high catalytic activity of material.    DETAILED DESCRIPTION - Preparation of carbon-coated titanium carbide loaded with nickel and cobalt tetroxide material comprises:    (A) taking 1x 10 cm titanium alloy sheet into tubular furnace, introducing 5% hydrogen and nitrogen, heating at 5-10 degrees C/minute to 60 degrees C for 2 hours, heating to 800-850 degrees C, introducing acetone for 120 minutes and cooling to room temperature to prepare carbon-coated titanium carbide nanowire array;    (B) taking carbon-coated titanium carbide nanowire array as working electrode, platinum electrode as counter electrode, saturated calomel electrode as reference electrode, 0.1-0.3 mol/L cobalt nitrate and 0.1-0.3 mol/L triethanolamine as electrolyte, electrodepositing at 0.01-3 V for 10-30 minutes;    (C) soaking in ethanol and water solvent at 70-30:30-70 volume ratio, carrying out in-situ growth with 0.2-0.5 mol/L oxalic acid for 2-5 hours; and    (D) drying at 250-350 degrees C for 4-5 hours.
NOVELTY - Fischer-Tropsch synthesis gas reaction of biomass involves filling solid catalyst into fixed bed reactor containing hydrocarbon liquid fuel, performing gas-solid reaction at 180-230 degrees C under pressure of less than 1 MPa, and collecting by direct water cooling. The solid catalyst contains primary metal catalyst and carrier. The metal catalyst is cobalt catalyst. The carrier is mono-oxide or composite oxide. The promoter metal is chosen from rhenium, ruthenium, copper, magnesium, zirconium or platinum.    USE - Fischer-Tropsch synthesis gas reaction of biomass (claimed).    ADVANTAGE - The method enables Fischer-Tropsch synthesis gas reaction of biomass with conversion rate of 90%, by simple method.
NOVELTY - The method involves heating solid organic matter raw material for thermal decomposition reaction. A pyrolysis reactor and a gaseous product are generated in a moving bed gasification reaction device for a gasification reaction with steam to produce hydrogen rich gas. A pyrolysis reaction device is connected with a moving bed gasification reaction device. A solid heat carrier is divided into two parts based on grain size. The pyrolysis reaction device is provided with a fluid-bed pyrolyzing reactor and a moving bed pyrolysis reactor.    USE - Method for producing steam gasification of solid organic substance hydrogen-rich gas.    ADVANTAGE - The method enables realizing normal pressure operation and simple technique to ensure high volatile co-gasification and co-gasification of organic matter in an effective manner.    DETAILED DESCRIPTION - The solid organic matter raw material is biomass, high molecular solid waste, coal and petroleum. The biomass is selected from cellulose, hemicellulose and lignin.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing steam gasification of solid organic substance hydrogen-rich gas.'(Drawing includes non-English language text)'
NOVELTY - Preparing cinacalcet hydrochloride comprises (i) taking 3-(trifluoromethyl)phenylpropionaldehyde and R-1-(1-naphthyl)ethylamine as raw material, mixing and reacting in presence of reaction solvent and sodium triacetoxyborohydride, performing condensation and reduction reaction; (ii) extracting the reaction product with aqueous solution of salt or alkali to obtain cinacalcet base organic phase solution; and (iii) acidifying cinacalcet base organic phase solution with hydrochloric acid to obtain cinacalcet hydrochloride, where one component in the reaction solvent is water.    USE - The method is useful for preparing cinacalcet hydrochloride (claimed).    ADVANTAGE - The method utilizes aqueous reaction solvent, which overcomes the technical prejudice of sodium triacetoxyborohydride, avoids rigorous conditions, improves the reaction selectivity, reduces the types of impurities generated and impurity content, reduces the cost, and is environmentally friendly.
NOVELTY - The utility model claims one using PEIC anaerobic reactor device's nitrogen gas, comprising a nitrogen replacing pipe, three control valves and three-way, between the PEIC gas-liquid separator is connected with a PEIC's upper marsh gas anaerobic tank air inlet pipe, the gas inlet pipe are respectively provided with one control valve upper sludge return pipe, the control valve PEIC anaerobic tank are respectively connected with three-way, three-way is connected with nitrogen pipe, nitrogen replacement is connected nitrogen source. The utility model greatly shortens the PEIC anaerobic reactor emptying time, and capable of being replaced hydrogen sulphide gas and combustible gas PEIC tank's weight, and nitrogen and low cost.
NOVELTY - Fracturing fluid comprises 0.5-2 pts. wt. phosphate thickener, 0.1-1 pts. wt. cross-linking agent and 100 pts. wt. butane.    USE - Used as a fracturing fluid.    ADVANTAGE - The fluid has thermal resistance and shear resistance performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fracturing fluid, comprising subjecting butane gas to -10 to -30 degrees C environment to obtain liquid butane, adding phosphate thickener and cross-linking agent into liquid butane and stirring uniformly at -10 to -30 degrees C to obtain primary product (without breaker), adding phosphate thickener, aqueous breaker and cross-linking agent into liquid butane and stirring uniformly at -10 to -30 degrees C to obtain primary product (with breaker), transferring primary product into pressure-proof air-tight container at room temperature and stirring using magnetic stirrer for 10-40 minutes.
NOVELTY - The biomass gasification furnace has a fan (1) that is connected with a gasification furnace (4) through the air inlet pipes (2,3). The gasification furnace is connected with a filter (5). The filter is connected with an exhaust switch (6), an exhaust pipe (7) and an air storage tank (8). The air storage tank is connected with a gas stove (9), an air distribution switch (10) and a tar discharging switch (11).    USE - Biomass gasification furnace used in household application.    ADVANTAGE - The combustible gas can be obtained effectively for cooking and warming applications by heating agricultural waste material in the gasification device. The utilization rate of biomass gasification furnace can be improved efficiently. The energy-saving efficiency of biomass gasification furnace can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification furnace.    Fan (1)    Air inlet pipe (2,3)    Gasification furnace (4)    Filter (5)    Exhaust switch (6)    Exhaust pipe (7)    Air storage tank (8)    Gas stove (9)    Air distribution switch (10)    Tar discharging switch (11)
NOVELTY - The method involves heating animal and plant oil in a horizontal rotating kettle. The heated animal and plant oil is entered into a fixed bed cracking reactor for performing a catalytic cracking reaction. Low hydrocarbon gas is separated from the animal and plant oil by a stable tower liquid and gas water oil separator. The gas separated from the animal and plant oil is heated by a pump pipe-type corrosion resistant heating furnace and entered in a rectifying tower for obtaining biological petrol, jet coal, biological diesel oil and biological fuel oil.    USE - Method for producing clean fuel from animal and vegetable oil by a catalytic cracking hydrogenation process.    ADVANTAGE - The method enables avoiding pollution to an environment caused by combustion products. The method enables avoiding utilization of strong acid and concentrated alkaline low carbon alcohol during combustion products production process and improving environmental and economic benefits.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for producing clean fuel from animal and vegetable oil by catalytic cracking hydrogenation process.
NOVELTY - The device has a tank body (1) provided with a tank cover (2), an air combustion-supporting chamber (11) and a heat-resistant layer (12). An outer wall ring of the heat-resistant layer is connected with a gas storage chamber (13). An inner wall surface ring of the gas storage chamber is provided with multiple air holes (14). An upper part of the gas storage chamber is provided with an air outlet joint (15). A lower part of the air outlet joint is provided with a water outlet (16). The heat-resistant layer is sleeved on an air passage (17).    USE - Biomass fuel gas gasification device.    ADVANTAGE - The device ensures better continuity and reliability of the tank body.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fuel gas gasification device.    Tank body (1)    Tank cover (2)    Air combustion-supporting chamber (11)    Heat-resistant layer (12)    Gas storage chamber (13)    Air holes (14)    Air outlet joint (15)    Water outlet (16)    Air passage (17)
NOVELTY - Additive comprises 5-20% butanone, 3-10% OP-10, 7-30% ethylhexyl nitrate, 10-22% solvent oil, 8-30% dimethyl carbonate, 6-21% ethyl ether, 1.5-2.5% ethylene oxide, 0.5-2% T551 antioxidant, 0.5-2% T501 antioxidant, 0.5-1% T1201 antioxidant, 4-8% methyl tertiary butyl ether, 3-7% isopropyl alcohol and 4-13% tertiary butyl alcohol.    USE - The additive is useful for preparing methanol-gasoline (claimed).
NOVELTY - Additive comprises 7-10 pts. wt. high-alkali ethanolamine, 12-17 pts. wt. propanol, 12-18 pts. wt. formaldehyde, 9-13 pts. wt. compatibilizer, 10-14 pts. wt. preservative, 6-9 pts. wt. detoxifying agent, 7-11 pts. wt. dehydrating agent, 5-10 pts. wt. butyl acetate, 3-8 pts. wt. tetrachloroethylene, 1-4 pts. wt. sudan-1, and 1-8 pts. wt. aromatic hydrocarbon.    USE - The additive is useful for modifying methanol gasoline and as vehicle fuel additive (all claimed).    ADVANTAGE - The additive compounds and modifies methanol; overcomes poor and difficult ignition of low temperature methanol, which causes difficulty in starting the car under low temperature; and improves dynamic performance of methanol fuel, which can reduce corrosion of automobile parts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the additive, comprising pre-dissolving and pre-mixing the above mentioned raw materials, shearing and dispersing, allowing to stand and aging.
NOVELTY - Normal temperature fine desulfurizing low-sulfur-containing natural gas comprises contacting low sulfur-containing natural gas and iron oxide fine desulfurizing agent, then contacting modified activated carbon with fine desulfurizing agent to obtain desulfurized natural gas.    USE - The method is useful for normal temperature fine desulfurizing low-sulfur-containing natural gas (claimed).    ADVANTAGE - The method performs alkali-free operation and oxygen-free operation; has simple and economical operation process; consumes less energy; and produces natural gas without obvious smell, and achieves total sulfur content according to the national standard or industrial standard.
NOVELTY - Bio-energy block, prepared by crushing farmland straw, adding household waste, inoculating anaerobic bacteria, and pressing and taking out block-shaped object.    USE - Used as a bio-energy block.    ADVANTAGE - The block is convenient to transport, conserve natural environment, achieves the purpose of waste recycling, and creates large quantity of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the bio-energy block.
NOVELTY - The utility model claims a household biomass gasification device technology field, especially relates to one kind of upper-suction biomass gasification furnace. It comprises an inner tube, the inner tube upper part is connected with the air outlet pipe, a furnace bracket and furnace wall, the furnace wall of the upper part is provided with a wind upper cover, the upper cover through the transverse air outlet hole and the inner air tube is connected with an ash through an ash bracket is set on the furnace wall of the lower part of upper part is provided with an ash upper fire grate and lower fire grate, a three-way pipe is set on the upper fire grate and lower fire grate upper, the upper part is provided with a wind cover, wherein the upper cover and the air supply spiral conveying rod, outer end of the piston rod is provided with a spiral conveying spiral conveying connecting rod and spiral conveying handle, a spiral conveying rod is set up with a hopper, and the it can satisfy all kinds of common's biomass gasification, can measure time gasification reaction temperature change's of each reaction zone, so as to know the temperature of the gasification reaction's reaction. The combustion is stable, the heat efficiency is high.
NOVELTY - The utility model claims one by using solid organic material for producing chemical raw material gas's device, the device comprises a material pre-processing module, a material powder module, a material conveying module, a gasification module, a discharging module, a washing module and water processing module through one series of processing to generate chemical raw material gas. The device can use most of coal, biomass straw and solid organic waste chemical raw material gas, and recovering the generated in gasification process's waste heat, and solves chemical raw material gas with ash band's serious problem can be common organic matter generate chemical raw material gas, meets related factory.
NOVELTY - The utility model claims one for laying the biomass fuel gas pipeline upper purifying and separating tar's device. Said tar catcher comprises one round table-shaped barrel body, said barrel body is provided with a round table-shaped air inlet, an oil discharging port, exhaust port, said round table-shaped barrel body is provided with catching tar component, said air inlet and air outlet are connected with the flange, the oil outlet is provided with a sealing cover and the round table-shaped lower end. The utility model's beneficial effects: with the existing tar catcher compared, capturing tar component is composed of several guide, capture mainly the tar for tar component, the structure is more simple, the oil tar collecting together, it changes waste into valuable.
NOVELTY - The utility model claims one's grading diversified A biomass fuel gas purifying device. Comprises one box body, said box body is composed of a plurality of square barrel body is divided into two layers, the body's positive upper part is fixed with a pressure equalizer through the water conveying pipe, a pressure equalizer upper part is connected with a water inlet pipe, a box body's upper right angle side is provided with an air inlet hole connecting flange, the left upper angle top is provided with an exhaust hole connecting flange, the air inlet hole and air exit hole's box on the top part is equipped with a pressure gauge and temperature detection bar, left corner's box exhaust valve in said multiple square barrel body and barrel body's left corner are provided with an observation window and a plurality of spraying device, and is provided with a clapboard in the last one barrel body, multiple plate combined water-gas separator, a water level control switch is located at the bottom and gap's box body under the clapboard's exhaust hole is formed at one's sealed in the water tank, a drain pump is connected with pipe is set in the water groove. The utility model is featured with simple structure, good purification effect.
NOVELTY - In one of biomass gasification furnace, comprising a furnace body (1), a furnace body (1) is a double-layer, the furnace body (1) is a combustion chamber (2), a combustion chamber (2)'s inner wall is coated with a refractory material layer (3), a furnace body (1), the lower part is provided with a clapboard (4), the corresponding position is further provided with a slag outlet (5), a combustion chamber (2) in the clapboard (4)'s lower part is equipped with air supply pipe (6), a blast pipe (6) and fan (7). The advantages are as follows: the water, low heat value's garbage, the roughing, the furnace gasification processing, the temperature of the furnace basically stable at 850 degrees C to 1100 degrees C degrees centigrade, 900 degrees C, the flue gas reaches the national discharge standard, and detecting all percolate in the furnace is no sewage discharge, at the same time, the fuel gas and the fuel oil. Realize " three-chemical " processing garbage, creatively embodying the processing waste, energy and protect environment's triple.
NOVELTY - The utility model claims's main part up for charcoal bar making machine, the out section from the front end, middle part and back end is connected with spiral section sections, middle part spiral section by section and pushing section, wherein the pushing side of the base circular surface's spiral part upper section is welded with a reinforcing belt, said main shaft part is composed of mould steel chromium. This utility model adopts said technical solution, the welding pushing force reinforcing band, improves connecting intensity's spiral part and the base circle portion, so as to improve the charcoal bar making machine's and improves the production efficiency; the main shaft component is composed of chromium steel mould and improves the temperature resistance and wear resistance, and the 45 # steel's main shaft component, prolongs the service life thereof is 4-6.5 times, so as to reduce the maintenance and reduces the production cost. the side surface's spiral part up pushing section with the base circular surface
NOVELTY - The device has a gas cooker (2) connected with a biogas generator (1) and provided with a pipeline (3). A vertical filter tank (32) is placed on the gas cooker that is provided with a fuel gas inlet (31). The filter tank is provided with an upper water discharging valve (4).    USE - Biomass gas filtering device.    ADVANTAGE - The device can maintain pressure at constant state so as to ensure normal use of the cooker.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gas filtering device.    Biogas generator (1)    Gas cooker (2)    Pipeline (3)    Upper water discharging valve (4)    Fuel gas inlet (31)    Vertical filter tank (32)
NOVELTY - The method involves switching a flow path switching valve to a flow analysis path and a flow channel. Hydrogen is analyzed in a marsh gas. Methane is analyzed in a single integral detector to obtain a relative concentration of the hydrogen. A sample inlet is connected with a two-position ten-way valve in a serial manner. The two-position ten-way valve is arranged with a sample gas taking quantitative ring. The two-position ten-way valve is connected to the flow analysis path. The flow path is connected with a shunt valve group. The ten-way valve is connected to a zirconium oxide detector.    USE - Marsh gas methane and hydrogen detecting method.    ADVANTAGE - The method enables realizing constant hydrogen and constant methane in single detector integral analysis process, avoiding signal amplification and stabilizing a circuit and increasing reliability and accuracy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a marsh gas methane and hydrogen detecting method.'(Drawing includes non-English language text)'
NOVELTY - Water-catalytic processing of hydrogen involves heating the water to generate steam, producing negative ions with metal catalyst and electrolyzing water vapor to generate hydrogen.    USE - Water-catalytic processing of hydrogen used in fuel cells.    ADVANTAGE - Process simplifies the hydrogen production process, thus effectively reducing the hydrogen preparation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the electrolytic device comprising a container between the load and fuel cell, hydrogen storage container (40), fuel cell (30), hydrogen fuel generator, catalytic hydrogen generating device, electrolyte container (20), water storage container (10), heating device (42) and carbon nanotube filling absorber.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the water-catalytic processing of hydrogen.    Water storage (10)    Electrolyte container (20)    Fuel cell (30)    Hydrogen storage (40)    Heater (42)
NOVELTY - An amisulpride acid is prepared by oxidizing 2-methoxy-4-amino-5-ethylthio-benzoic acid under alkaline condition.    USE - Preparation of amisulpride acid (claimed).    ADVANTAGE - Preparation process has improved yield, high-quality product, convenient operation, and safe and environment-friendly process.
NOVELTY - Carfentrazone-ethyl is synthesized by adding acetonitrile or butanone reaction solvent into reactor, passing nitrogen gas into reactor, controlling temperature to - 10-0 degrees C, adding 1-(5-amino-2-fluoro-4-chlorophenyl)-3-methyl-4-(difluoromethyl)-1H-1,2,4-triazol-5-one and copper(I) chloride while continuously stirring for 20-50 minutes, adding dropwise concentrated hydrochloric acid and ethyl acrylate, controlling temperature to 0-5 degrees C, adding dropwise tert.-butyl nitrite diazotizing reagent, performing reaction for 20-100 minutes, and performing distillation under atmospheric pressure.    USE - Synthesis of carfentrazone-ethyl (claimed).    ADVANTAGE - Synthesis process is environment-friendly and has high selectivity, short reaction time, and high product yield.    DETAILED DESCRIPTION - Carfentrazone-ethyl is synthesized by adding acetonitrile or butanone reaction solvent into reactor, passing nitrogen gas into reactor, controlling temperature to - 10-0 degrees C, adding 1-(5-amino-2-fluoro-4-chlorophenyl)-3-methyl-4-(difluoromethyl)-1H-1,2,4-triazol-5-one and copper(I) chloride while continuously stirring for 20-50 minutes, adding dropwise concentrated hydrochloric acid and ethyl acrylate, controlling temperature to 0-5 degrees C, adding dropwise tert.-butyl nitrite diazotizing reagent, performing reaction for 20-100 minutes, performing distillation under atmospheric pressure to recover solvent and unreacted ethyl acrylate, diluting ethyl acrylate, performing filtration to obtain copper(I) chloride, and evaporating impurity at 110-125 degrees C under 15-20 mmHg.
NOVELTY - Quercetin is extracted from green tea waste by pulverizing dried green tea leaves through 80 mesh sieve, transferring to Soxhlet extractor, adding petroleum ether which is 51 times amount of dried tea leaves, reflux for 3 hours, removing cartridge filter and drying in air, pre-processing with 40-60% ethanol with solid-to-liquid ratio of 1:25-30, uniformly stirring for 2 hours, microwave extracting for 6-10 minutes, centrifuging, collecting supernatant, vacuum concentrating, and recrystallizing in solvent twice.    USE - Extraction of quercetin from green tea waste (claimed).    ADVANTAGE - The extraction of quercetin from green tea waste is simple, fast, efficient, energy-saving, environment-friendly, suitable for industrialized production, uses less solvent, and has high purity product.
NOVELTY - A synthetic fuel contains 75-85% methanol, 0.3-0.9% dicyclopentadienyl iron, 0.3-0.7% aluminum powder, 1.5-5% preservative, and 12-22% gasoline.    USE - Synthetic fuel for motor vehicle (claimed).    ADVANTAGE - The synthetic fuel has simple process, low cost, and available raw material, is environment-friendly, safe, sanitary, and energy-saving, and avoids poisoning accident.
NOVELTY - The portable gas detection apparatus (10) comprises a gas detection element (12) that measures the concentration of gas and transmits a gas concentration signal. A control unit (16) receives the gas concentration signal and generates a display signal regarding the gas concentration and measuring time. A display (13) receives the display signal and displays the time series graph of the gas concentration. A power supply (18) drives the gas detection element, control unit and the display. A function sets the threshold value of the gas concentration manually.    USE - Portable gas detection apparatus for detecting gas, such as hydrogen, oxygen, carbon monoxide, carbon dioxide, propane, butane, methane and for measuring the gas concentration in atmosphere. Can also be used for monitoring the time-sequential change of the gas concentration of operation atmosphere.    ADVANTAGE - The portable gas detection apparatus comprises a display that receives a display signal and displays the time series graph of the gas concentration, and thus easily displays the time-sequential change of gas concentration, realizes the portable gas detection apparatus even if the power supply is incorporated without connecting with the external power supply, effectively detects the gas leakage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a portable gas detection apparatus. (Drawing includes non-English language text).    Portable gas detection apparatus (10)    Gas detection element (12)    Display (13)    Control unit (16)    Power supply (18)
NOVELTY - An ammonia-treated biomass (S1) is obtained by treating cellulosic biomass using an ammonia-containing treatment agent. An ammonia-treated biomass is immersed into a solvent containing at least water, and a coumaramide is eluted in the ammonia-treated biomass in the solvent, to obtain coumaramide solution (S2). The coumaramide is deposited in the coumaramide solution as a crystal, to obtain coumaramide crystal (S3).    USE - Manufacture of coumaramide used for producing chemical product.    ADVANTAGE - The method efficiently provides coumaramide with high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart explaining the manufacture of coumaramide. (Drawing includes non-English language text)    Ammoniation biomass process (S1)    Obtaining coumaramide solution (S2)    Obtaining coumaramide crystal (S3)
NOVELTY - Method for producing of biofuel comprising bioethanol involves (a) pressing grass to obtain grass juice, (b) separating liquid from the grass juice, (c) pasteurizing the liquid, (d) acidifying and incubating the liquid, and (e) fermenting the liquid to produce biofuel including bioethanol.    USE - The method for producing of biofuel (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biofuel prepared by the above-mentioned method; and    (2) precipitate having fatty acid composition as provided in table 1 of patent specification, and amino acid composition as provided in table 2 of patent specification.
NOVELTY - The system comprises two devices (10,20) that are used for setting the torrefaction grades by cutting and homogenizing the biomasses (B1,B2) before torrefaction of biomass (B).    USE - System for torrefaction of biomass.    ADVANTAGE - The torrefaction of biomass can be performed in simple and environmental-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawings show the graph illustrating the torrefaction of biomass and schematic view of the system for torrefaction of biomass.    Sleeve shaft (3)    Devices (10,20)    Pipeline (11)    Intake port (21)    Biomasses (B,B1,B2)
NOVELTY - A composition comprises graphite particle having solid content ratio of 70-80 mass%, and resin component, where the graphite particle comprises particle group with powder resistance of 3.0 m(ohm) cm or less under average particle diameter of 25-100 micrometers and pressure of 30 Mpa.    USE - Composition for manufacturing fuel cell separator that is utilized in fuel cell (all claimed).    ADVANTAGE - The composition has better moldability, better fluidity and provides fuel cell separator with high electro-conductivity, improved productive efficiency, improved heat resistance improved durability, improved electrical resistibility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a fuel cell separator    (2) a method for manufacturing fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of unit cell of fuel cell.    Channel (2)    Membrane-electrode composite body (5)    Gasket (12)    Cathode side separator (21)    Anode side separator (22)    Oxidizing agent electrode (31)    Fuel electrode (32)
NOVELTY - Preparing memantine hydrochloride, comprises: (a) reacting 1,3-dimethyladamantane with acetonitrile in presence of sulfuric acid at a temperature of 25-45 degrees C in absence of solvent; (b) isolating obtained 1-acetamido-3,5-dimethyladamantane with the addition of water; (c) hydrolyzing 1-acetamido-3,5-dimethyladamantane with base in presence of aqueous isobutanol at a temperature of 110-140 degrees C to give memantine free base; (d) in-situ treating memantine free base with hydrochloric acid at a temperature of 5-35 degrees C and completely distilling out aqueous isobutanol and adding ester solvent.    USE - The process is useful for preparing memantine hydrochloride (claimed) for treating Alzheimer's and Parkinson's disease. No biological data given.    ADVANTAGE - The improved process: produces memantine hydrochloride with more than 99.9% purity; is eco-friendly and plant-friendly and commercially viable; involves fewer operations in the preparation of memantine hydrochloride; reduces process operation stages hence saving the manufacturing cost, manpower and time cycles; can avoid generation of unwanted excessive effluent; uses less equipments; and avoids purification step.
NOVELTY - A recombinant yeast microorganism comprising at least one exogenous gene and/or at least one overexpressed endogenous gene encoding an enzyme that catalyzes a pathway step in the conversion of pyruvate to isobutanol, where the recombinant microorganism is engineered to reduce the expression and/or activity of at least one endogenous lactate-cytochrome-c-reductase, is new.    USE - The recombinant yeast microorganism is useful for producing isobutanol (claimed), fuels, chemicals, and amino acids.    ADVANTAGE - Recombinant microorganisms which are engineered to reduce the expression and/or activity of at least one endogenous lactate-cytochrome-c-reductase for improved production of fuels, chemicals, and amino acids are provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of producing isobutanol comprising: (a) providing a recombinant microorganism; and (b) cultivating the recombinant microorganism in a culture medium containing a feedstock providing a carbon source, until the isobutanol is produced.
NOVELTY - Converting organic material into biogas comprises treating the organic material with an enzyme composition comprising a hemicellulase and a pectinase to reduce the viscosity of the organic material, followed by a fermentation to produce the biogas.    USE - The enzyme composition is useful for converting an organic material into biogas by reducing the viscosity of the organic material, where the organic material includes plant material and greater than 30 wt.% of rye (all claimed), and the biogas includes methane, carbon dioxide and hydrogen sulfide.    ADVANTAGE - The improved chemical, enzymatic and/or microbial method is capable of economically treating all kind of digestible organic material with reduced viscosity, improved pumping properties and less slime formation under lower stirring energy condition.
NOVELTY - Producing saccharified solution comprises: obtaining mixture containing saccharified solution and undecomposed biomass residue obtained by treating substrate biomass using saccharification enzyme; and obtaining saccharified solution as filtrate by filtering mixture using filtration unit, where step of producing saccharified solution further comprises before filtering mixture using filtration unit, adjusting 95 mass% or more of particles, based on total amount of particles contained in centrifuged supernatant obtained after mixture is centrifuged as to have a particle size of 1-30 mu m.    USE - The process is useful for producing saccharified solution.    ADVANTAGE - The process: provides saccharified solution practically free of the undecomposed biomass residues in high filtration yield; and requires less energy to perform filtration, thus reducing production cost.
NOVELTY - Biogas reactor comprises: two reel-mixers in a container (1) with an encircling cylindrical wall (2), a first container preservation beer end having a first section, which extends from one shaft to the other shaft, is perpendicular to the two shafts, and pass through the cylinder axis surrounded by the cylindrical wall and a second section. The shafts of the two reel mixers are aligned approximately parallel to one another. The second section extends from each shaft to an inner side of the wall.    USE - Used as a biogas reactor.    ADVANTAGE - The biogas reactor: allows an efficient mixing of the biomass to be fermented; improves the stirring efficiency; and can be manufactured in simple and inexpensive manner.    DETAILED DESCRIPTION - Biogas reactor comprises: two reel-mixers in a container (1) with an encircling cylindrical wall (2), a first container preservation beer end having a first section (A), which extends from one shaft to the other shaft, is perpendicular to the two shafts, and pass through the cylinder axis surrounded by the cylindrical wall and a second section (B). The shafts of the two reel mixers are aligned approximately parallel to one another. The second section extends from each shaft to an inner side of the wall. The arrangement of two shafts in the container fulfills the equation ((first section) divide by 2 is equal to Kx second section), in which K is a factor having a value of more than 1.    DESCRIPTION OF DRAWING(S) - The figure shows a top view of a biogas reactor (Drawing includes non-English language text).    First section (A)    Second section (B)    Container (1)    Wall (2)    Bottom (3)
NOVELTY - Producing dimethyl ether, comprises (a) fermenting biomass for producing crude biogas containing methane and carbon dioxide, (b) cleaning the crude biogas by separating carbon dioxide to obtain a methane-enriched crude biogas, (c) producing synthesis gas comprising carbon monoxide and hydrogen by reacting methane with oxygen, and (d) producing dimethyl ether from the synthesis gas by catalytic condensation of the synthesis gas or from the synthesis gas as methanol, which is condensed in the intermediate step.    USE - The method is useful for producing dimethyl ether.    ADVANTAGE - The method: is carried out in a cost efficient manner; and produces reduced byproducts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a production plant for producing dimethyl ether comprising a fermenter, a crude biogas purifier for the separation of methane and carbon dioxide, a synthesis gas reactor, and a dimethyl ether reactor for catalytic condensation of synthesis gas to dimethyl ether.
NOVELTY - Initiating biogas plant (1) for producing an inoculum concentrate, comprises: (a) generating a filtrate stream from a filtrate; (b) feeding the filtrate into a reactor charged with filling body; (c) generating the inoculum concentrate in the reactor; (d) removing the inoculum concentrate from the reactor; and (e) discharging the filtrate from the reactor.    USE - The method is useful for initiating biogas plant for producing an inoculum concentrate.    ADVANTAGE - The method is simple and produces highly concentrated inoculum concentrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant for carrying out the above method, comprising at least one filtrate duct, and reactor equipped with filling bodies, which is connected with the filtrate duct.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method for initiating biogas plant.    Biogas plant (1)    Biogas reactor (2)    Valve (3)    Pump (4)    Filter (7)
NOVELTY - This utility model claims a kind of fertilizer production device, comprising a connected according to the order of the granulator, a drying machine, a transmission device and a packaging machine, wherein the transmission device comprises a conveying belt, wherein two sides of the conveyor belt is provided with the fertilizer particles falling from the belt, said transmission belt is provided with a bracket, the bracket of the cross rod is provided with multiple cooling fan. The advantages of the utility model is: it not only can prevent particle scattering in the transmission process, and the fertilizer particle is uniform, the belt damage, which greatly improves the production efficiency and the service life of the conveyer belt.
NOVELTY - Preparation of non-steroidal antiinflammatory drug tolmetin (I) comprises taking N-methyl pyrrole as raw material, reacting with oxalyl chloride monoethyl ester in the presence of toluene, acid-binder, triethylamine and sodium hydroxide; condensing with ethyl acetate solution; condensing with methyl-benzoyl chloride; and reacting with sodium hydroxide, bleaching with activated carbon, acidifying, filtering, washing and drying.    USE - Method for preparing non-steroidal antiinflammatory drug tolmetin (claimed).    ADVANTAGE - The method reduces pollution and production cost.    DETAILED DESCRIPTION - Preparation of non-steroidal antiinflammatory drug tolmetin of formula (I) comprises:    (A) taking N-methyl pyrrole as raw material to obtain (1-methyl-1H-pyrrol-2-yl)-oxo-sodium acetate of formula (iii);    (B) reacting with oxalyl chloride monoethyl ester in the presence of toluene, acid-binder, triethylamine and sodium hydroxide to obtain N-methyl pyrrole -2- acetate of formula (iv);    (C) condensing with ethyl acetate solution to obtain 3-(1-methyl-1H-pyrrol-2-yl)-2-oxo-propionic acid methyl ester of formula (v);    (D) condensing with methyl-benzoyl chloride to obtain (1-methyl-5-(4-methyl-benzoylamino)-1H-pyrrol-2-yl)-acetic acid methyl ester of formula (vi); and    (E) reacting with sodium hydroxide, bleaching with activated carbon, acidifying, filtering, washing and drying.
NOVELTY - Potassium oxonate is synthesized by dissolving allantoin in potassium hydroxide aqueous solution or potassium carbonate aqueous solution, and reacting with aqueous solution of hypohalite and oxidizing agent under potassium iodide catalyst.    USE - Synthesis of potassium oxonate (claimed).    ADVANTAGE - The process is simple with mild reaction and environment-friendly and has high product yield with high purity.
NOVELTY - A barasertib 2-(5-((7-3-(ethyl(2-hydroxyethyl)amino)propoxy)quinazolin-4-yl)amino)-1H-pyrazol-3-yl-N-(3-fluorophenyl)acetamide is prepared by performing condensation reaction of 7-(3-(ethyl(2-hydroxyethyl)amino)propoxy)-quinazolin-3,4-dihydro-4-one and (5-amino-1H-pyrazole)-3-yl-N-(3-fluorophenyl)acetamide.    USE - Preparation of barasertib 2-(5-((7-3-(ethyl(2-hydroxyethyl)amino)propoxy)quinazolin-4-yl)amino)-1H-pyrazol-3-yl-N-(3-fluorophenyl)acetamide (claimed).    ADVANTAGE - Preparation process is simple and environment-friendly and has mild condition.    DETAILED DESCRIPTION - A barasertib 2-(5-((7-3-(ethyl(2-hydroxyethyl)amino)propoxy)quinazolin-4-yl)amino)-1H-pyrazol-3-yl-N-(3-fluorophenyl)acetamide compound of formula (I) is prepared by performing condensation reaction of 7-(3-(ethyl(2-hydroxyethyl)amino)propoxy)-quinazolin-3,4-dihydro-4-one and (5-amino-1H-pyrazole)-3-yl-N-(3-fluorophenyl)acetamide.
NOVELTY - Synchronization of alkaline earth metal oxide catalytic biodiesel oil and glycerol carbonate comprises adding natural oil, dimethyl carbonate and methanol into reaction kettle, adding 5-20% solid alkaline powder, stirring and heating at 50-90 degrees C for 4-8 hours, cooling to room temperature, filtering, washing, evaporating filtrate to obtain light yellow liquid which is the biodiesel oil crude product, extracting with equal volume of methanol for 2-4 times and removing methanol to obtain glycerol carbonate. The natural oil is mixture of acid, dehydrated vegetable oils and animal oils.    USE - Method for synchronizing alkaline earth metal oxide catalytic biodiesel oil and glycerol carbonate (claimed).    ADVANTAGE - The method uses oxides as catalysts which have low cost, high catalytic activity and easy separating process to reduce processing cost.    DETAILED DESCRIPTION - Synchronization of alkaline earth metal oxide catalytic biodiesel oil and glycerol carbonate comprises adding natural oil, dimethyl carbonate and methanol at mass ratio of 1:(1-5):(1-10) into reaction kettle, adding 5-20% solid alkaline powder, stirring and heating at 50-90 degrees C for 4-8 hours, cooling to room temperature, filtering, washing, evaporating filtrate to obtain light yellow liquid which is the biodiesel oil crude product, extracting with equal volume of methanol for 2-4 times and removing methanol to obtain glycerol carbonate. The natural oil is mixture of acid, dehydrated vegetable oils and animal oils. The solid alkaline powder is calcium oxide, barium oxide, magnesium oxide, calcium oxide-magnesium oxide-barium oxide composite oxide, aluminum oxide or magnesium oxide-aluminum oxide composite oxide.
NOVELTY - A feces sphingosine bacilli Sphingobacterium faecium ZJF-D6 (CCTCC M2013251) is new.    USE - Feces sphingosine bacilli Sphingobacterium faecium ZJF-D6 (CCTCC M2013251) for D-allose production, and medicine.    ADVANTAGE - The feces sphingosine bacilli Sphingobacterium faecium ZJF-D6 (CCTCC M2013251) is stable, low cost, efficient, highly selective, and environment-friendly. Preparation reduces use of organic solvent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Sphingobacterium faecium ZJF-D6 (CCTCC M2013251).
NOVELTY - The utility model claims a fertilizer production device, specifically to a long-acting high tower compound fertilizer for producing double-prilling tower, comprising a tower and tower, wherein the tower is provided with a secondary lifting machine, wherein the main column is provided with a shell and a pelleting spray head is connected with a shell, wherein the unit is provided with the conical tower above the air inlet of the air distribution plate, the air distribution plate is the inner cavity of the tower is divided into two chambers, the use of said structure, the utility model is the one kind of long-acting high tower compound fertilizer production and can reduce and granulated by a double-tower and the dust generated, the particle fertilizer in doping impurities, reduce environmental pollution, improves the production quality of the fertilizer, and it avoids the waste of raw material.
NOVELTY - This utility model belongs to synthesis ammonia production technology field, especially relates to a kind of synthetic ammonia system machine parallel system, comprising a first stage, a second stage synthesis ammonia system of low temperature methanol washing and air pump for ice and synthesizing ammonia with ice machine, comprising a first stage, a second stage synthetic ammonia system the first, the second and the third sides of a liquid ammonia storage tank, washing at low temperature for the first period and second period methanol and synthetic ammonia system for space division ice machine and the first section, second section inlet gas ammonia pipeline and the outlet is provided with a pipeline, at the same time, is connected with the upper pipeline is equipped with a valve in each of a low temperature methanol washing liquid ammonia pipeline of the synthetic ammonia to the first period and second period synthetic ammonia system with ice and the first section, second section inlet gas ammonia pipeline and an outlet gas ammonia pipeline and also connected with a pipeline, at the same time, is connected with the upper pipeline is equipped with a valve. This utility model stable production, saves energy source and improves energy utilization rate, reduces the device consumption, reduce the production cost and increase the economic benefit of enterprises, improve the atmospheric environment, the enterprise market competitive power, which meets the national development requirement of the enterprise is energy-saving and environment-friendly, suitable for popularization.
NOVELTY - This utility model claims a kind of a municipal domestic garbage aerobic fermentation process of rotating cylinder type bioreactor, comprising a spiral feeding device, a spiral discharging device, the reactor cylinder, a gear wheel supporting device, the catch wheel supporting device, a transmission device, a feeding box and a discharging box. Spiral feeding device enter into the reactor cylinder is conveying material at the same time, the material of the mixing. The inner wall of the reactor from the inlet end to the outlet end of the three type shovelling plate, wherein the spiral pushing shovelling plate material is pushed into the reactor cylinder, parallel shovelling stable reading the material, the material is completely time and space to be carried out aerobic fermentation, residence time of the resistance material shovelling plate extend material compound composed of blocking part and a parallel part is formed by injection molding, the material further. The utility model is provided with material stirring more fully, the aerobic ferment more completely.
NOVELTY - This utility model claims a kind of structure is simple, the operation is convenient, the cost is low for the rapid temperature-rising device of high temperature and aerobic composting fermentation. This utility model is realized by the following way: organic fertilizer fermenting workshop roof solar heat collecting tube a (hot), making heat water tank ferment workshop, the hot water of the heat collecting station stored in the hot water tank. Lifting ground timed fermenter for laying geothermal pipe net, water pump for circulating the hot water tank to heat water to the geothermal pipe net, the ferment slot temperature via hot water.
NOVELTY - The utility model claims an aerobic compost air oxygen supply system, a plurality of composting a stack in a fermenting workshop is provided with a fermentation tank or fermentation chamber, a stack fertilizer bar buttress, a fermenting tank or fermenting chamber are provided with vent-pipe and guide pipe, each pipe is connected with a vent-pipe, a guide pipe is connected with a guide pipe, the pipe wall of the vent pipe close to the air corresponding to the air outlet is set with a between the two is set with gas/gas heat exchanger, a ventilation pipe and the pipe wall close to the total air pipe is set with a between the two is set with gas/gas heat exchanger, or corresponding to the guide pipe is sleeved on the outer side of the vent-pipe, there is a gap between the two, a guide pipe is sleeved on a vent pipe, there is a gap between the two. This utility model can be used to stack waste heat air and supply air to do heat exchange, the aerobic compost stack on the premise of not increasing the heat energy or electric energy of the air inlet temperature, reduces the stack of the aerobic air inlet temperature of the bad interference and improve the aerobic rate, shortens the fermentation period.
NOVELTY - This utility model claims a full-automatic fast high-temperature compost fermentation, comprising a fermentation tank main body and a motor, wherein the fermentation tank main body and electric motor are fixed on the machine base, the fermentation tank main body of the tank wall is double-layer structure, the inner layer wall and the outer layer tank wall is filled with heat preservation material, the fermentation tank main body top part is provided with an automatic heat preservation; fermentation tank main body is further provided with a circulating fan, a circulating blower fan main body is provided with a fermentation tank, fermentation tank main body top part on the inner side wall of the cover is provided with a far infrared heating tube is provided with a stirring device in the fermentation tank main body is equipped with an automatic heat preservation material outlet close to the fermentation tank for fermentation tank main body that the bottom of the main body of box wall. This utility model has high heating efficiency, high fermentation efficiency, flexible adjustment and can reduce the labour cost.
NOVELTY - This utility model claims a kind of pleurotus eryngii production using corn core pre-wetting stirring device, comprising a pre-wet tank, the pre-wet tank is connected with the stirring tank, the upper part of the stirring tank is provided with a water compensating device, the stirring tank of the box body are provided with rotating shaft, the rotating shaft is fixed is set with a stirring paddle, the stirring paddle in spiral shape around the rotating shaft, the utility model is advantages as follows: it can avoid the long training material pre-wet time, the water content reduce acid to induce saccharification so as to cause the problem of the stirring pre-wet time, good effect, improves the working efficiency and production quality.
NOVELTY - Manufacture of biodiesel involves adding microalgae to a solvent containing microalgal biodiesel, swelling oil droplets, extracting bio-oil containing swollen oil droplets, performing trans-esterification and purifying.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The biodiesel is economically produced from microalgae without affecting the environment.
NOVELTY - Separating and recovering hydrochloric acid and gallic acid using reverse osmosis membrane technology, comprises separating hydrochloric acid and gallic acid mother liquor after filtration through ultra filtration and nanofiltration at a certain temperature and pressure conditions to obtain concentrated solution with no gallic acid and hydrochloric acid as main penetrating liquid, concentrating liquid by cooling and crystallizing, and then centrifuging to obtain gallic acid and hydrochloric acid, where the temperature is 20-80 degrees C, and the pressure is 20-44 bar.    USE - The method is useful for separating and recovering hydrochloric acid and gallic acid using reverse osmosis membrane technology (claimed).    ADVANTAGE - The method rapidly separates and recovers hydrochloric acid and gallic acid with low energy consumption in an environmental friendly and economical manner.
NOVELTY - Livestock injection comprises rhizoma coptidis and slow-release auxiliary material.    USE - As livestock Coptis injection (claimed).    ADVANTAGE - The injection has improved sustainability in animal blood, improves efficacy of drugs, and reduces the impact of stress caused by drugs in animals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the injection, which involves crushing Coptis into coarse powder, adding 8 times of solvent for refluxing and extracting for two times, where each time the extraction is performed for 1 hour, filtering and combining the filtrates, recycling compound solvent, concentrating the filtrate into paste and dissolving in hot water, filtering and recovering ethanol from filtrate to adjust the pH value to 1-2, adding 10 wt.% salting-out agent to the paste, uniformly shaking the obtained mixture, standing for 24 hours, filtering and washing by water until the pH value is 5, heating to dissolve the mixture, adding 0.1% activated carbon to the obtained mixture, heating and boiling for 20 minutes, cooling and filtering the obtained mixture, spray-drying to obtain powder, adding slow-release auxiliary material, and packing the product.
NOVELTY - Preparation of organic fertilizer from red grape pruning branches comprises crushing red grape pruning branch; mixing 100 lbs crushed material with 10 lbs chicken manure and 0.10 lbs bio-fermenting agent; piling up each stack of about 3000 kg dry branches and fresh branches at ratio of 30:25 while allowing uniform flow of water; turning pile once every 6 days; and piling up for 15-20 days at less than 15 degrees C to convert into fertilizer.    USE - Preparation of organic fertilizer from red grape pruning branches (claimed).    ADVANTAGE - The method can change waste into valuable product, and saves red grape per acre garden fertilizer costs of 300 Yuan. It produces organic fertilizer that provides comprehensive nutrition to crops, has long fertilizer efficiency, increases organic matter in soil, promotes microorganism propagation, improves physical and chemical properties and biological activity of soil, and promotes growth of crop and yield.
NOVELTY - The device has a mixing stirrer (10) that is provided for mixing and stirring the raw materials uniformly. A crusher (20) is arranged in a granulator (30), for crushing the large agglomeration material. The crushed material is directly entered into the granulator. A slurry distribution mechanism (40) is provided for spraying liquid material on a material bed. The granulator is provided for granulating the dried material dried by a drying machine (50). A pre-neutralizing tail cleaning machine (80) is provided for generating the pre-neutralizing slurry.    USE - Fertilizer production device.    ADVANTAGE - The product quality, uniformity and yield of fertilizer production device can be improved. The sewage discharge of fertilizer production device can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fertilizer production device. (Drawing includes non-English language test)    Mixing stirrer (10)    Crusher (20)    Granulator (30)    Slurry distribution mechanism (40)    Drying machine (50)    Pre-neutralizing tail cleaning machine (80)
NOVELTY - Special fertilizer for ornamental flower plant, comprises 25-35 wt.% Trichoderma, 15-20 wt.% urea, 12-13 wt.% ammonium dihydrogen phosphate, 12-13 wt.% potassium oxide, 6-13 wt.% attapulgite powder, 10-15 wt.% humic acid, and 1-2 wt.% amino acid chelated rare earth.    USE - As Special fertilizer useful for ornamental flower plant.    ADVANTAGE - The Special fertilizer has excellent water retention ability and ventilation property for long period of time, is suitable for growth and cultivation of plant roots, as the plant absorbs phosphorus, enables to prevent ammonia, and potassium loss, soil mineral to fix into plant active ingredient, and promote growth of crops.
NOVELTY - A compound fertilizer comprises seaweed extract, chitosan oligosaccharide and microbial agents.    USE - A compound fertilizer.
NOVELTY - Ganoderma lucidum cultivation material comprises 25-35 wt.% tea seed meal, 20-30 wt.% tea dust, 20 wt.% bagasse, 15 wt.% rice bran, 5 wt.% tea seed oil meal, 2 wt.% corn flour, 1 wt.% gypsum powder, 1 wt.% lime powder, and 1 wt.% calcium superphosphate, on dry basis.    USE - Ganoderma lucidum cultivation material (claimed).    ADVANTAGE - The cultivation material uses tea seed meal processed by a process which efficiently removes toxic bacteria and degrades macromolecular substance, which provides excellent absorption property. Ganoderma lucidum growth is improved, good ventilation property is provided, water-preservation property is strengthened. Cultivation yield is improved by 13.4-14.2% and production cost is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (i) manufacture of cultivation material, which involves drying and mixing tea seed meal, tea dust, and bagasse, dissolving lime powder in water, pre-wetting the mixture for 2 hours, maintaining the water content of mixture at 50-55%, mixing rice bran, tea seed oil meal, corn flour, calcium superphosphate, and gypsum powder, pre-wetting the mixture, slowly adding water, stirring while adding the bagasse mixture, setting water content to 63-65%, filling 17 cmx 35 cmx 0.005 cm polypropylene bags with 1100-1200 g mixture/bag, covering, sterilizing at atmospheric pressure at 100 degrees C, maintaining for 10-12 hours, and cooling to 25 degrees C or less; and (ii) Ganoderma lucidum cultivation method, which involves inoculating with strain, placing cultivation bags in dark room, controlling temperature at 22-24 degrees C and humidity at 60-75%, culturing for 30-32 days, and budding in outdoor shade.
NOVELTY - An effective microbial population improved soil comprises invalidation-type phosphorus, potassium and other trace elements, effective phosphorus and potash fertilizer.    USE - Effective microbial population improved soil (claimed).    ADVANTAGE - The plant root grown using the effective microbial population improved soil has improved disease resistance, stress resistance and drought resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for improvement method of effective microbial population in soil, which involves sterilizing microbial population, adding 20 times of water, providing the resultant product into special sealing barrel, culturing at 25-35 degrees C for 3-5 days, adjusting pH to 3.8 to obtain secondary generation of effective microbial population, adding sugar mud, sugar, powdered rock phosphate, potassium mineral powder, nitrogenous fertilizer, soybean, food industrial waste, rice bran, wooden meal, wheat bran, animal excrement and crop roots, providing resultant product into a tank, stirring, sealing, then carrying out anaerobic fermentation at 20-30 degrees C for 10-15 days to obtain tertiary generation of effective microbial population, mixing obtained 20-35 kg/acre resultant product with farmyard manure and organic fertilizer, maintaining soil wet, deeply-plowing the soil, uniformly mixing strain, seedling, carrying out tiller the resultant product, booting and spraying.
NOVELTY - A (R)-(+)-1-(1-naphthyl)ethylamine is prepared by mixing tartaric acid and methyl alcohol-water mixed solvent, adding alkaline solution to adjust pH to 9-12, extracting with ethyl acetate and concentrating.    USE - Method for preparing (R)-(+)-1-(1-naphthyl)ethylamine (claimed).    ADVANTAGE - The preparation has high product yield, low cost and is environment-friendly.
NOVELTY - Preparing erlotinib hydrochloride crystal form B involves reacting erlotinib as raw material with hydrogen chloride in presence of solvent, cooling, and crystallizing to obtain erlotinib hydrochloride crystal form B. The erlotinib is a single crystal, a crystal or amorphous solid. The hydrogen chloride is hydrochloric acid or hydrogen chloride gas. The reaction solvent is the mixture of acetone or acetone and water.    USE - For preparing erlotinib hydrochloride crystal form B (claimed) which is useful as anti-tumor medicine.    ADVANTAGE - The preparation method is simple; is suitable for industrial production; does not use toxic solvent; has no pollution to the environment; has product purity of more than 99%; and has yield of more than 95%.
NOVELTY - Synthesis of 5-azaindole involves: 1) oxidizing 3-methyl pyridine under the influence of oxidant to give 3-methyl pyridine nitrogen oxide; 2) nitrating 3-methyl pyridine nitrogen oxides in mixed acid to give 3-methyl-4-nitro pyridine nitrogen oxide; 3) reacting 3-methyl-4-nitro pyridine nitrogen oxides and phosphorus trichloride in a solvent to give 3-methyl-4-nitro-pyridine; 4) reducing 3-methyl-4-nitro-pyridine in a solvent to give 3-ethenyl-4-dialkylamino-nitropyridine; and 5) cyclizing 3-dialkylamino vinyl-4-nitropyridine in metal catalyst to give 5-azaindole.    USE - For synthesis of 5-azaindole (claimed) used for the treatment of cardiovascular disease, inflammation, central nervous system disorders and diseases such as diabetes mellitus.    ADVANTAGE - The method is of low cost, has small environmental pollution, and has high industrial feasibility.    DETAILED DESCRIPTION - Synthesis of 5-azaindole using 3-methyl pyridine as raw material, involves: 1) oxidizing 3-methyl pyridine under the influence of oxidant to give 3-methyl pyridine nitrogen oxide; 2) nitrating 3-methyl pyridine nitrogen oxides in mixed acid to give 3-methyl-4-nitro pyridine nitrogen oxide; 3) reacting 3-methyl-4-nitro pyridine nitrogen oxides and phosphorus trichloride in a solvent to give 3-methyl-4-nitro-pyridine; 4) reacting and reducing 3-methyl-4-nitro-pyridine in a solvent under heating conditions to give 3-ethenyl-4-dialkylamino-nitropyridine; and 5) cyclizing 3-dialkylamino vinyl-4-nitropyridine metal catalyst under reduction reaction to give the final product of 5-azaindole.
NOVELTY - A cultivation substrate comprises 30-40 pts. wt. sawdust, 5-10 pts. wt. sweet potato, 10-20 pts. wt. wheat bran, 5-15 pts. wt. bagasse, 8-15 pts. wt. beans, 5-10 pts. wt. corn starch, 10-30 pts. wt. straw, 3-6 pts. wt. shell fossil, 5-8 pts. wt. calcium carbonate, 15-20 pts. wt. mushroom bran, 2-3 pts. wt. carbide, 5-10 pts. wt. soybean curd, and 5-8 pts. wt. lees.    USE - A cultivation substrate used for Pleurotus eryngii (claimed).    ADVANTAGE - The cultivation substrate provides balanced nutrition to P. eryngii.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the cultivation substrate, comprising crushing sweet potato to obtain sweet potato residue; mixing with sawdust, wheat bran, bagasse, beans, corn starch, straw, shell fossil, calcium carbonate, mushroom bran, carbide, soybean curd, and lees; and adding water, stirring, controlling humidity at 65-68%, placing in a cultivation flask, and sterilizing.
NOVELTY - Treatment of aquatic livestock and poultry comprises cleaning aquatic livestock and poultry corpse, decomposing into double-wall boiler, heating at 300-500 degrees C, adding oil into double-wall boiler of double layer furnace wall, sterilizing wastewater, processing sewage, filtering feces, fermenting and producing organic fertilizer; and filtering, barreling, and producing biodiesel.    USE - Method of treatment of aquatic livestock and poultry (claimed).    ADVANTAGE - The method is safe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the treatment of aquatic livestock and poultry.
NOVELTY - The utility model claims a comprehensive using cold energy of liquefied natural gas for ammonia synthesis device, wherein the device comprises a heat exchange unit, a raw material is natural gas of the air unit (6), adjusting the raw synthesis gas components for rectifying and separating unit (5), wherein a first LNG storage tank in the low-temperature LNG liquid heat exchange heating gasification through the heat exchange unit, the input unit and the input gas is steam, air to generate coarse synthesis gas, raw synthesis gas by changing heat exchange after cooling, a rectifying and separating unit, and adjusting the ratio of the raw synthesis gas a gas obtaining fine synthesis gas from the ammonia synthesis unit outside the tower top to the boundary zone, bottom product for redundant cold recycling, waste gas is conveyed to a fuel system, a methane and hydrogen as fuel. This utility model claims a cold energy of LNG is coupled to the cryogenic purification process of ammonia gas, releasing a LNG gasification negative influence to the environment, compressor, expander and assisting refrigeration process is further greatly save electric energy and cooling water.
NOVELTY - This utility model claims a chain type dumper, comprising a vehicle walking part, a driving device, a turning component, an electric control system device, the large vehicle walking part comprises a vehicle frame and walking part, wherein the walking part is installed on the big frame lower part, the electric control system device and a driving device is installed on the large vehicle frame, and the turning part is installed on the big bottom of the frame, the driving device comprises a walking driving device and a turning driving device, the walking driving device is connected with the walking part, the turning driving device is connected with a turning part connected with the walking component driving device is a hydraulic driving device, the hydraulic driving device comprises an oil tank, a motor, an oil pump, a control valve, a hydraulic motor and a hydraulic cylinder. According to a control system device and a device electrically connected with the circuit board. The utility model runs stably, turning rate is high, it can carry out deep operation, can effectively shorten the fermentation period, improves composting quality.
NOVELTY - The utility model claims a kind of organic waste resource enzyme rapid thermal processor, comprising: the heat enzyme treatment reactor according to bearing seat (1), a stuffing box (2), a stirrer (3), a machine cover (4), a filter screen of the air outlet (5), a clamp (6), an electric control cabinet (7), a heating control mixing tank (8), the discharging butterfly valve (9) with a brake pulley (10), limit switch (11), a draught fan (12), a speed reducer (13), chain transmission (14), a variable frequency motor (15), the utility model has simple structure and it is easy to manufacture, it is convenient to operate and maintain, high temperature control, the rotating speed can be adjusted, uniformly mixing is suitable for microorganism enzymolysis to ferment, preparing organic fertilizer; Suitable for processing organic waste in family, community, factory, farm, restaurant, farm products market, park and so on.
NOVELTY - Based on ecological cycle agricultural system of rural waste anaerobic fermentation, comprising a straw crusher to crush the straw and crushing the leftover food leftover food grinder, a discharging opening of the straw crusher is connected with the feeding port by movable conveying belt and the solar energy fermenting house one of the outlet of the crusher is connected with the leftover food through a feeding port of the movable conveying belt and the solar fermentation room II, the solar fermentation room is respectively connected with a penetrating fluid tank, a substrate processing room is connected with the leftover food, pig manure and penetrating fluid and water, river water, and the solar fermentation room II and filtrate pool are connected with the stacking fermented mixed to a liquid tank is connected with the slurry tank and the biogas tank to carry out anaerobic fermentation to mixed material generate anaerobic marsh gas tank and connected with the anaerobic tank is connected with the biogas liquid temporary storage, a marsh gas purifying chamber for purifying biogas, the biogas liquid tank and the water sprinkling a marsh liquid pool field connected with the marsh gas purifying chamber and the marsh gas generator for self-supplying power supply.
NOVELTY - This utility model belonging to the technical field of solid waste treatment, especially relates to a kind of sludge compost turning machine. The machine body part is provided with the cab and the roof platform, two sides of the bottom of the machine body is provided with a walking system, machine body is further set with lifting transmission system, a shaft lifting transmission system is connected, the rotation axis a plurality of arranged along the cross spiral of the spiral turning plate and a plurality of axially arranged along radial direction of the turning plate through a bearing, a temperature detection point in the bearing, a humidity detection point, a oxygen content detection point. Turning throwing plate design can ensure the rolling uniformity for splashing at the same time, direction and speed of uniformly, so as to ensure the sludge stack is substantially level, a detection point, a motor operating current, frequency and other parameters in real time is transmitted to a test point monitoring device PLC and human-machine interface in the cab HMI on the display, and a self-adjusting running power of the walking speed and the rotating shaft.
NOVELTY - The system has material tank (3), feed supplement tank (2) and overflow tank (11) that are connected with a reaction tank (7) through a pipeline. The reaction tank is provided with heat-insulating jacket. The heating device (16) and refrigerating unit (4) are connected with heat-insulating jacket. An ultrasonic generator (10) is provided at bottom of reaction tank. A reaction tank is provided with a stirring device (5) which is driven by electric motor. The stirring rod and stirring blade are located on feed supplement tank, mixing tank and reaction tank.    USE - Safe disposal and recycling system for energetic material used in propellant (claimed) for aerospace, military application, army, navy and air force application and other personal weapons.    ADVANTAGE - The energetic material is incinerated, such that the waste material can be used as fertilizer for the agricultural production, so as to eliminate the landfill waste material and environmental pollution and economic benefit for agricultural production can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a realizing method of safe disposal and recycling system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the safe disposal and recycling system for energetic material.    Feed supplement tank (2)    Material tank (3)    Refrigerating unit (4)    Stirring device (5)    Reaction tank (7)    Ultrasonic generator (10)    Overflow tank (11)    Heating device (16)
NOVELTY - Manufacturing selenium-enriched wheat aqueous biological organic fertilizer involves mixing 98-99 wt.% of soybean, 0.3-0.7 wt.% of sodium selenite, 0.1-0.8 wt.% of bacillus, 0.1-0.5 wt.% of crude fiber degrading bacteria, as premix; adding 50-65 wt.% of water; fermenting it at 55-60 degrees C for 45-50 days to generate no smell, brown, pink surface mycelium full maturity state, adding 0.05-0.1 wt.% of aka amine hexanoate (DA-6) to the fermentation, adding 1-5 wt.% of starch grafted crosslinked acrylate copolymer, and uniformly mixing, extruding and granulating.    USE - For manufacturing selenium-enriched wheat aqueous biological organic fertilizer (claimed).    ADVANTAGE - The selenium-enriched wheat aqueous biological organic fertilizer has accurate dosage; has high fertilizer effect; and increases wheat yield by 10-15%.    DETAILED DESCRIPTION - Manufacturing selenium-enriched wheat aqueous biological organic fertilizer involves mixing 98-99 wt.% of soybean, 0.3-0.7 wt.% of sodium selenite, 0.1-0.8 wt.% of bacillus, 0.1-0.5 wt.% of crude fiber degrading bacteria, as premix; adding 50-65 wt.% of water; fermenting it at 55-60 degrees C for 45-50 days to generate no smell, brown, pink surface mycelium full maturity state, adding 0.05-0.1 wt.% of aka amine hexanoate (DA-6) to the fermentation, adding 1-5 wt.% of starch grafted crosslinked acrylate copolymer, and uniformly mixing, extruding and granulating through a circular particle diameter of 0.3-0.45 mm.
NOVELTY - A mushroom cultivation material comprises 25-35% of chestnut tree meal, 22-28% of corn meal, 15-19% of oak chip, 20% of corn cob, 5% of bran, 1% of gypsum powder, and 2% of lime powder.    USE - As mushroom cultivation material (claimed).    ADVANTAGE - The mushroom cultivation material removes the toxic bacteriostatic substances; reduces the macromolecular substance; is beneficial to the absorption, and hypha growth; has reasonable proportioning, good air permeability, strong water-retaining property, and effectively mushroom quantity; has biological efficiency of 130.2-140.5%; and greatly reduces the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the mushroom cultivation material involving mixing the raw materials for 1-2 days before insolation, using ultraviolet rays to kill the bacteria in the material part, prewetting the chestnut tree, corn meal, oak chip in a dry state under uniform stirring, carrying out pre-wet with 2% of lime water solution (wet completely), stacking ferment the wet material piling height is 1-1.2 m, the width is 2-3 m, and the length is not limited to ladder-shaped stack, each stack of cultivation in a dry weight of 300-500 kg, and a diameter of 10-15 cm of the stick of the stack on some vertical air hole through the stack, at last cover the upper part of the tarpaulin to make it natural ferment, turning, when the material temperature reaches 60 degrees C, keeping for 24 hours, then carrying out, and after a days turning stack a sequence, at the third time, adding corn core, bran, gypsum powder and auxiliary material, and the water content of stack material adding water, turning time is 4-5 times, and the time for 6-7 days, and stopping fermenting, where the culture material has water content of 63-65%.
NOVELTY - A Tricholoma lobayense seed culturing material comprises 60-70 wt.% corn, 18-28 wt.% rice grain, 10 wt.% bacteria slag, and 2 wt.% gypsum powder.    USE - Tricholoma lobayense seed culturing material.    ADVANTAGE - The method improves water holding capacity of the culturing material and prolongs strain storage life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of culturing material comprising soaking corn in 0.5% lime water for 15-20 hours, washing with water, putting into pot, cooking until white heart line, and drying; washing rice, germinating at 25 degrees C, dipping in 0.5% lime water solution, putting in boiling water pot to kill rice sprout, and drying; drying bacteria slag and gypsum powder, mixing, pre-wetting for 2 hours, and keeping water content to 58-60%; mixing with corn and rice grains, putting into 1100 mlx 78 mm polypropylene plastic bottle, and covering with ventilating sponge bottle cap; and sterilizing at 100 degrees C for 1 hour, heating to 121 degrees C for 2 hours, and naturally cooling at 25 degrees C.
NOVELTY - Extracting psoralen and isopsoralen based on cloud point extraction comprises mixing fructose psoralae powder with surfactant solution, extracting under ultrasonic conditions, collecting extract, centrifuging to separate into two phases, collecting supernatant, adding electrolytes to adjust ionic strength, heated in water bath, equilibrating, in which two phases are supernatant phase which is aqueous phase of surfactant, and surfactant-rich layer, membrane filtration of surfactant-rich layer, recycling surfactant, spin drying filtrate to obtain fat soluble crude extracts.    USE - Used for extracting psoralen and isopsoralen (claimed).    ADVANTAGE - Extraction method does not use harmful organic solvents, has increased extraction rate, reduces environment pollution and is suitable for large scale extraction.
NOVELTY - Forming tenofovir (I) involves reacting 6-chloro-5-nitro-pyrimidin-4-ylamine (II) with (R)-4-methyl-(1,3)dioxolan-2-one, then subjecting (R)-4-methyl-(1,3)dioxolan-2-one to ring-opening condensation reaction to obtain (R)-4-(N-(2-hydroxypropyl)amino)-5-nitro-6-chloro-pyrimidine (III), performing reduction cyclization of the compound (III) to obtain (R)-1-(6-chloro-purin-9-yl)-2-propanol (IV), subjecting the compound (IV) to ammonolysis reaction to obtain (R)-1-(6-amino-purin-9-yl)-2-propanol (V), followed by etherification and hydrolysis.    USE - For the preparation of tenofovir (claimed) which is used for the treatment of human immunodeficiency virus (HIV) and hepatitis B virus (HBV) infection.    ADVANTAGE - The method utilizes easily available raw materials; is simple, cost-effective and environment-friendly, thus suitable for industrial production.    DETAILED DESCRIPTION - Preparation of tenofovir of formula (I) involves: reacting 6-chloro-5-nitro-pyrimidin-4-ylamine (II) with (R)-4-methyl-(1,3)dioxolan-2-one, then subjecting (R)-4-methyl-(1,3)dioxolan-2-one to ring-opening condensation reaction to obtain (R)-4-(N-(2-hydroxypropyl)amino)-5-nitro-6-chloro-pyrimidine (III), performing reduction cyclization of the compound (III) to obtain (R)-1-(6-chloro-purin-9-yl)-2-propanol (IV), subjecting the compound (IV) to ammonolysis reaction to obtain (R)-1-(6-amino-purin-9-yl)-2-propanol (V), followed by etherification and hydrolysis.
NOVELTY - A strain, preferably Bacillus amyloliquefaciens NJAUYL-25 (CGMCC N0 7626) for promoting growth of banana, is new, where the NJAUYL-25 strain is Gram-positive, rod-shaped cells, spore-forming, and aerobic, shows positive result for catalase test, gelatin hydrolysis test, voges proskauer test, starch hydrolysis, and nitrate reductase test, and negative result for methyl red test, is capable of fermenting glucose, sucrose, dextrin, mannitol, xylose, arabinose, and does not ferment lactose.    USE - The strain, preferably B.amyloliquefaciens NJAUYL-25 useful for promoting growth of banana and preparing microbial organic fertilizer (all claimed).    ADVANTAGE - The strain, preferably B.amyloliquefaciens NJAUYL-25 enables to improve growth of banana to 45.6-122.0%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial organic fertilizer; and    (2) method for preparing the microbial organic fertilizer.
NOVELTY - A genetically engineered bacteria of Streptomyces autolyticus (CCTCC M 2013156), is new.    USE - The genetically engineered bacteria is useful for fermentative production of autolysis of penicillin (all claimed) which is used for providing antitumor effect.    ADVANTAGE - The genetically engineered bacteria enables to improve yield and is environmentally-friendly.
NOVELTY - This utility model claims a method for manufacturing organic fertilizer of animal compost, wherein the device is composed of open rotten room to ferment, activate nutrient solution supply unit, a drying unit, a cooling filtering unit, a discharging unit and a fertilizer effect adjusting unit, the apparatus comprising a yeast for animal manure of the rotten chamber, further provided with a nutrient solution activated activated nutrient solution supply unit is a rotten, prepared a discharge opening leading to a drying unit, a drying unit to the rotating drying unit of high temperature and livestock manure of livestock manure sieving, cooling effect of the cooling screen unit, a cooling filtering unit after connected with the spiral discharging unit. This utility model quickly droppings. decomposed livestock excrement to short time on medium rotten organic fertilizer, the mechanization operation can effectively save the labour cost and time, so as to effectively improve the decomposing efficiency, and it has wide application value.
NOVELTY - Banaba special base fertilizer and its preparation method, are claimed. The fertilizer comprises 32-34 wt.% dry manure, 16-18 wt.% dry dairy manure, 5 wt.% rapeseed cake, 10 wt.% straw, 10 wt.% polluted river mud, 5 wt.% mildew feed, 1 wt.% organic fertilizer fermentation agent, 1 wt.% deodorant, 6 wt.% amino acid liquor, 4 wt.% monoammonium phosphate, 6 wt.% potassium chloride, 0.4 wt.% humic acid chelated iron, 0.3 wt.% humic acid chelate copper, 0.4 wt.% humic acid chelated calcium, and 1 wt.% plant growth regulator.    USE - The banaba special base fertilizer is useful for providing drought, pest and disease resistance and improving immunity.    ADVANTAGE - The fertilizer is rich in organic matter, inorganic matter and humic acids and chelated trace elements, odorless, sterile and easy to use, activates roots in soil to absorb nutrients.    DETAILED DESCRIPTION - Banaba special base fertilizer and its preparation method, are claimed. The fertilizer comprises 32-34 wt.% dry manure, 16-18 wt.% dry dairy manure, 5 wt.% rapeseed cake, 10 wt.% straw, 10 wt.% polluted river mud, 5 wt.% mildew feed, 1 wt.% organic fertilizer fermentation agent, 1 wt.% deodorant, 6 wt.% amino acid liquor, 4 wt.% monoammonium phosphate, 6 wt.% potassium chloride, 0.4 wt.% humic acid chelated iron, 0.3 wt.% humic acid chelate copper, 0.4 wt.% humic acid chelated calcium, and 1 wt.% plant growth regulator. The fertilizer is prepared by placing dry pig manure, dry dairy manure, rapeseed cake, straw, polluted river mud, and mildew feed into a crusher for crushing, placing the crushed product into a fermenting tank, adding the organic fertilizer fermentation agent and water into the fermentation tank and mixing uniformly, sealing and fermenting for 20-22 days and adding amino acid liquor, sterilizing, then uniformly stirring and drying till the water content is less than 3%, crushing the remaining raw materials, mixing them uniformly to obtain the finished product.
NOVELTY - An intelligent control system comprises control unit, programmable controllers, liquid level control device, material conveying device, fermentation device, filling device, sewage treatment device, ultrasonic wave sensor, sewage pump, fumigation control device, turning mechanism, transmission belt and temperature sensor.    USE - Intelligent control system used for biofertilizer production (claimed).    ADVANTAGE - The system has simple structure, convenient usage, no pollution and adopts automatic filling method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of intelligent control system (Drawing includes non-English language text).
NOVELTY - Forming urea involves passing discharge air through pressure regulator valve, adjusting pressure of ammonia supplied, washing with air in wash column, controlling pressure of ammonia to pressure of 1.2-1.5 MPa, washing with soft water detergent, after washing passing through exhaust vent, returning resulting ammonia to intermediate pressure column, using detergent to wash ammonia, where mass% of ammonia concentration is 5-7%, passing portion of ammonia water into analytical system for recovery of ammonia, and passing ammonia and detergent softener to medium pressure ammonia washing tower.    USE - For producing urea using discharge air processing method (claimed).    ADVANTAGE - The discharge air used in the urea production has ammonia content of less than 5 mg/l. The ammonia can be effectively recycled, which not only saves the resources but also reduces the environmental pollution and provides economic and social benefits.    DETAILED DESCRIPTION - Producing urea using discharge air processing method involves passing discharge air through pressure regulator valve, adjusting pressure of ammonia supplied, washing with air in wash column, controlling pressure of ammonia washed in the washing column to a pressure of 1.2-1.5 MPa, washing with soft water detergent, after washing passing through exhaust vent, returning the resulting ammonia to the intermediate pressure column, using a detergent to wash the ammonia, where the mass percentage of the ammonia concentration is 5-7%, passing portion of ammonia water into analytical system for recovery of ammonia, and passing ammonia and detergent softener to medium pressure ammonia washing tower.
NOVELTY - A seed culturing material comprises 85-90 wt.% corn, 9-14 wt.% mushroom residue, and 1 wt.% gypsum powder, where the mass ratio of dry matter is 100%.    USE - A seed culture material used for Agaricus blazei (claimed).    ADVANTAGE - The seed culture material has a prolonged strain storage life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the seed culture material, comprising:    (A) washing corn grains with clean water, soaking for 8-10 hours, changing lime water, and soaking for 8-10 hours;    (B) boiling corn grains, and drying;    (C) uniformly mixing bacteria slag dry gypsum powder, mixing with corn grains, adding water, and maintaining moisture content of bacteria slag at 63-65%;    (D) bottling the culture material in polypropylene plastic bottles marked with bacteria planting hole, and covering with a breathable cap sponge; and    (E) heating to 121 degrees C for 2 hours, sterilizing for 1 hour at 100 degrees C, and naturally cooling to less than or equal to 25 degrees C.
NOVELTY - Planting material comprises 50-60 wt.% of tea seed meal, 10-20 wt.% of fresh tea meal, 12 wt.% of corncob, 10 wt.% of wheat bran, 5 wt.% of Phellodendron, 2 wt.% of gypsum powder and 1 wt.% of lime powder.    USE - Used as planting material.    ADVANTAGE - The planting material is cost-effective, and has increased production of 30-40%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the planting material comprising drying the raw materials to exposure for 1-2 days, adding the raw materials using UV light, mixing the Pleurotus citrinopileatus, tea seed meal and fresh tea dust under dry state condition and uniformly stirring, carrying out pre-wet with 1% of lime water solution and then stacking and fermenting the wet material with a piling height of 1-1.2 m and width of 2-3 m, cultivating 300-500 kg of the stacked material with a diameter of 10-15 cm, turning the cultivated material at 60 degrees C for 24 hours and adding with corn core, bran, tea seed, Phellodendron, gypsum powder and auxiliary material, adding the stack material with water and turning for 4-5 times and fermenting for 6-7 days until the water content is 63-65%, bagging the fermented material into a polypropylene plastic bag, inserting the material into the plastic bolt and then sterilizing and cooling into a pot at 100 degrees C for 8-10 hours, and naturally cooling the sterilized material to 25 degrees C.
NOVELTY - A culturing material comprises 30-40 wt.% tea seed meal, 20-30 wt.% tea root meal, 20-24 wt.% sugar, 12 wt.% rice bran, 3 wt.% soybean meal, 2 wt.% gypsum powder, and 1 wt.% lime powder.    USE - Culturing material used for Hypsizigus marmoreus (claimed).    ADVANTAGE - The culturing material increases production by 25-35% and reduces production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cultivating material comprises exposing raw material to UV for l-2 days for ultraviolet killing of bacteria; dry mixing tea seed meal and tea root meal, uniformly stirring, pre-wetting with 1% lime water solution; piling wet material to a height of 1-1.2 m and width 2-3 m, controlling weight of each stack at 300-500 kg, inserting stick with a diameter of 10-15 cm to make air holes in the stack, covering upper part with tarpaulin and allowing natural fermentation; maintaining temperature at 60 degrees c for 24 hours, turning, turning once after 1 day, on the third turning adding bagasse, rice bran, soybean meal, and plaster powder, adding water, turning for 4-5 times for 6-7 days, stopping fermentation, maintaining moisture content of culture material at 63-65%; transferring 1100-1200 g wet material into each 17 cmx 35 cmx 0.005 cm polypropylene plastic bag, covering; sterilizing at normal pressure, discharging cooling gas when temperature reaches 100 degrees C, keeping for 8-10 hours, and naturally cooling to less than 25 degrees C.
NOVELTY - Preparing thiamine hydrochloride comprises (i) preparing hydrogen chloride gas by heating thiamine and concentrated hydrochloric acid, subjecting desorbed hydrogen chloride gas to cooling, drying and dehydration to obtain a hydrogen chloride gas; (ii) passing dehydrated hydrogen chloride gas into methanol solution to obtain methanol solution containing hydrochloric acid; and (iii) dropwise adding methanol solution containing hydrochloric acid into methanol solution of thiamine nitrate for reacting, filtering, washing, and drying.    USE - The method is useful for preparing thiamine hydrochloride (claimed).    ADVANTAGE - The method: can prevent use of highly toxic and dangerous chemical chlorosulfonic acid; reduces the environmental risk, which can improve the utilization rate of hydrochloric acid and thiamine hydrochloride with bulk density.
NOVELTY - Use of ionic liquid solid catalyst for isomerizing 4-8C n-alkane at a temperature of 120-250 degrees C, a pressure of 0.1-10 MPa for 0.1-20 hours, is claimed.    USE - The catalyst is useful for isomerizing 4-8C n-alkane (claimed).    ADVANTAGE - The catalyst has good stability, good activity, good selectivity and high reaction performance.    DETAILED DESCRIPTION - Use of ionic liquid solid catalyst for isomerizing 4-8C n-alkane at a temperature of 120-250 degrees C, a pressure of 0.1-10 MPa for 0.1-20 hours, is claimed. The catalyst is prepared by reacting 8 g of methyl imidazole and 30 ml of chlorobutane under a protection of nitrogen (N2) and refluxing for 24 hours, freezing the mixed solution at 7 degrees C for 12 hours to obtain crystal product and removing clear liquid and then extracting using ethyl acetate at 90 degrees C for 3 times to obtain extracted liquid, rotary evaporating the extracted liquid for 4 hours to remove water to obtain 1-butyl-3-methylimidazolium chloride, reacting 1-butyl-3-methylimidazolium chloride with 5 g of aluminum chloride and impregnating with 10 g of aluminum oxide.
NOVELTY - The utility model belongs to the field's domestic garbage treatment, in particular solar domestic garbage low temperature circulating retort workshop, comprising a solar energy system, a daily garbage low temperature dry distillation workshop, comprising a collecting system, a transmission system, capable of adjusting system and a monitoring system, refrigerant cantilever tower type solar energy, a hydraulic pump station, a flat angle tracker, the total control chamber, a refrigerant type solar tracker, a refrigerant pump station, a heating medium storage tank, boiler, change, distribution room, a power supply automatic switching switch and a national grid, which includes a low temperature circulating dry distillation tower, liquid pipe is connected with valve, an oil-water separator, pump pipe, a liquid connecting pipe, a liquid collector, a solid matter discharge port, the solid discharging switch, centrifuging and purifying process, heat medium pipe, a heat medium pipe insulating layer, storing tank, a heat medium pump, a heat medium return pipe, a heat medium pump outlet pipe; A feeding pipe, a vacuum machine, a liquid collector connecting pipe, gas collecting pipe, seat and lower dry distillation tower, distillation tower upper, gas and liquid dividing pipe, an emergency maintenance window, a condenser, a gas storage tank and a valve. The pattern has a high efficiency, classification, classification is easy, small land occupation, pollution, changing waste into valuable's.
NOVELTY - The system has a multi-air chamber air-distributing device (3) provided with multiple closed annular chambers. A gasification medium generating device (5) is connected with a feeding device (1) that is connected with a gasification furnace main body (2). The gasification furnace main body is connected with a dreg-discharging device (4). The gasification medium generating device is provided with an oxygen-enriched preparation device and a water vapor generating device. The multi-air chamber air-distributing device is equipped with a conical-shaped air distributor.    USE - Coal and biomass synthesis gas gasification system.    ADVANTAGE - The system realizes processing coal, wood cellulose and co-gasification of municipal solid waste, ensures better synergistic effect of the coal and biomass, and has wide raw material adaptability, high gasification speed and residual carbon, and is easy to control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a coal and biomass gasification co-preparation synthesis gas method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a coal and biomass synthesis gas gasification system.'(Drawing includes non-English language text)'    Feeding device (1)    Gasification furnace main body (2)    Multi-air chamber air-distributing device (3)    Dreg-discharging device (4)    Gasification medium generating device (5)
NOVELTY - The utility model claims one for processing machinery, especially relates to one kind of particles. A one, comprising a machine frame, said machine frame one end of other end of the upper is provided with a motor frame is provided with a preparation method of immobilization microbe granule device assembly through a transmission device drives said granule preparation assembly, said assembly comprises a ring mould granule preparation said ring mould is provided with a feeding port, the said ring end is equipped with a discharging port. This utility model has simple structure, which can be conveniently pressed into organic waste can be utility's particle fuel for replacing non-renewable coal's, which greatly improves the utilization ratio's's resource, effectively improves the environment-friendly benefit and economic benefit.
NOVELTY - Processing and recycling livestock and poultry breeding wastewater, comprises passing the livestock and poultry biogas slurry from an anaerobic reaction system to a biogas tank using a conventional method, transferring the biogas slurry in slurry adjusting tank to a storage tank for settling, separating and/or removing suspended substance, performing biological treatment to biogas slurry, passing the discharged biogas slurry into a effective microorganism (EM) tank, and then adding mixing agent, and performing strengthening treatment to mixed slurry or performing aerobic fungus process.    USE - The method is useful for processing livestock and poultry breeding wastewater (claimed).    ADVANTAGE - The method process and recycles livestock and poultry breeding wastewater with rapid decomposing, decoloring and deodorizing pollutant, comprehensive utilization, saving energy and reducing radiation emission in a cost-effective manner.    DETAILED DESCRIPTION - Processing and recycling livestock and poultry breeding wastewater, comprises passing the livestock and poultry biogas slurry from an anaerobic reaction system to a biogas tank using a conventional method, transferring the biogas slurry in slurry adjusting tank to a storage tank for settling, separating and/or removing suspended substance, performing biological treatment to biogas slurry in the biogas slurry adjusting tank and then discharging or processing the discharged biogas slurry by a standard-reaching exhaust, passing the discharged biogas slurry into a effective microorganism (EM) tank and then adding mixing agent, where the biogas slurry adjusting tank is connected to a microbial enhanced sequential batch reactor biogas pool, performing strengthening treatment to mixed slurry or passing the biogas slurry in the biogas slurry adjusting pool to a aerobic fungus culture tank for performing aerobic fungus process and then carrying out strengthening treatment.
NOVELTY - This utility model claims one kind of epidemic disease dead poultry harmless treatment device, which solves the epidemic disease dead poultry processing will be improper disease and environmental pollution, and the existing processing mode's high processing cost. Comprising upper and lower through's high temperature furnace chamber, high temperature furnace chamber top part is a livestock inlet, and the bottom is the substrate outlet, high temperature furnace chamber in turn is provided with a supporting grid plate's, cutting device, a multi-level crushing device, the side's high temperature furnace chamber with air inlet, air inlet is connected with the high temperature furnace chamber to provide combustion engine's hot air flow, the top's's high temperature furnace chamber is provided with an air outlet, the air outlet is connected with a solid component is separated from the air flow's cyclone separator, a cyclone separator's solid component corresponding to combustion engine fuel inlet. The device of this utility model has low cost, and by making use of air and the combustible substance as fuel and reduce the fuel's cost.
NOVELTY - Preparation of biological gasoline comprises crushing waste in container with water twice the amount of waste; carrying out hydrolysis at room temperature by adding 10 wt.% ZH-906 catalyst, ZH-369, 10 wt.% ZH-36P and 25 wt.% ZH-368 auxiliary agents, and 35 wt.% ZH-968 and 20 wt.% ZH-966 additives; and standing and filtering.    USE - Method for preparing biological gasoline from agricultural and forestry waste (claimed).    ADVANTAGE - The method has low cost and good stability. It is energy-saving and environment-friendly.
NOVELTY - Fuel mixture comprises 25-81 wt.% gasoline, 5-15 wt.% methanol and 4-5 wt.% additive.    USE - Fuel mixture.    ADVANTAGE - Fuel mixture has good intersolubility and good exhaust emissions.
NOVELTY - Preparation of pure cypress biomass particle fuel comprises screening cypress sawdust to obtain less than 3 mm powder; mixing with cedar shavings at 2.5:1 ratio; drying mixed material until 10-15% water content; cooling to 40-50 degrees C; mixing with cedar shavings at 4:1 ratio; granulating; and warehousing.    USE - Method for preparing pure cypress biomass particle fuel (claimed).    ADVANTAGE - The method has simple technique, less dust generation, low production cost, high molding rate and high yield. Biomass particle fuel is not easy to slag.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of pure cypress biomass particle fuel preparation (Drawing includes non-English language text).
NOVELTY - Production of pure cedarwood biomass particle fuel comprises drum screening cypress sawdust to remove bulk materials; mixing with cedar shavings at 2.5:1 in distribution hopper; rotary drying; rotary screening, turning fan ventilation, cooling to 40-50 degrees C, removing dust by magnet; collecting material in distributing bucket, mixing with cedar shavings at 4:1 ratio; granulating, spraying in master control machine at 90-95 degrees C and high pressure, compressing; and vibration sieving, recovering pulp by cloth bag, removing dust by dust collecting device and storing.    USE - Method for producing pure cedarwood biomass particle fuel (claimed).    ADVANTAGE - The method has simple technique, high molding rate, high yield and low production cost. Biomass particle fuel is not easy to slag.    DETAILED DESCRIPTION - Production of pure cedarwood biomass particle fuel comprises drum screening cypress sawdust to remove bulk materials; mixing with cedar shavings at 2.5:1 in distribution hopper; rotary drying until 10-15% water content; rotary screening, turning fan ventilation, cooling to 40-50 degrees C, removing dust by magnet; collecting material in distributing bucket, mixing with cedar shavings at 4:1 ratio; granulating, spraying in master control machine at 90-95 degrees C and high pressure, adjusting granulation process to 15-20 MPa, compressing at 1:4 ratio; and vibration sieving, recovering pulp by cloth bag, removing dust by dust collecting device and storing.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of pure cedarwood biomass particle fuel production (Drawing includes non-English language text).
NOVELTY - Removal of excess methanol in biodiesel production comprises placing crude ester in temporary storage tank, heating at 65-70 degrees C in softener heater, entering in flash off alcohol column, cooling, heating at 65-70 degrees C, transferring in falling film dealcoholation tower, cooling in ice brine cooler and collecting.    USE - Method for removing excess methanol in biodiesel production (claimed).    ADVANTAGE - The method has reduced production cost.
NOVELTY - Complex metal oxide catalyst comprises layered compounds composed of controllable anion intercalation with hydrotalcite precursor of catalyst.    USE - Complex metal oxide catalyst used for production of biodiesel (claimed).    ADVANTAGE - The catalyst is stable, environment-friendly and inexpensive, has good crystallinity, large specific surface area, and high catalytic activity. The method is short and simple and has high yield.    DETAILED DESCRIPTION - Complex metal oxide catalyst for production of biodiesel comprises layered compounds composed of controllable anion intercalation with hydrotalcite precursor of catalyst obtained by formula (CaxM2+(1-x-y)My3+(OH)2)y+(A)y/nx mH2O.    x=fixed value;    M2+,M3+=divalent and trivalent metal ions;    A=interlayer anion with anionic charge;    y=0.17-0.33;    M=l-Ny/n; and    N=number of position occupied by anion.    An INDEPENDENT CLAIM is included for preparation of complex metal oxide catalyst comprising mixing 0.1-5.0 mol/L divalent metal nitrate or sulfate or hydrochloride salt as solution A and 0.01-2.5 mol/L trivalent metal nitrate or sulfate or hydrochloride salt as solution B' at ratio of 2-4:1, adding deionized water to obtain solution C', dissolving sodium hydroxide, ammonia, potassium hydroxide, calcium hydroxide or urea in water to obtain solution D with concentration of 0.1-4.0 mol/L,, crystallizing under nitrogen atmosphere for 30 minutes to obtain precipitate, mixing solution C' and D at rate of 1-40 ml/minute for 3-10 hours by addition method, separating, filtering, washing, fast or slow drying to obtain hydrotalcite precursor, calcining at 500-800 degrees C in muffle furnace for 5-8 hours, milling and cooling.
NOVELTY - Treatment of domestic garbage comprises separating domestic garbage to obtain organic material and waste slag, carbonizing organic material to obtain solid residue and mixed gas, grinding solid residue, and cooling to obtain carbon-containing fuel; cooling mixed gas to obtain mixed oil, rectifying to obtain crude oil and gas, and cooling to obtain first class diesel oil; and sterilizing waste slag, adding fertilizer, mixing, and stirring to obtain modified soil.    USE - Method for treating domestic garbage (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of treatment of domestic garbage (Drawing includes non-English language text).
NOVELTY - This utility model claims one kind of multi-zone type bioreactor, comprising a reactor cylinder body, wherein, said reactor cylinder is a sleeve structure, comprising an outer cylinder and an inner cylinder, said inner cylinder's forming an anaerobic area, said outer cylinder and the inner cylinder to form the aerobic zone and settling zone, aerobic zone and said zone is separated by the baffle plate, said anaerobic zone is provided with a water distributor and a drain pipe, said water distributor and water inlet pipe is connected with said anaerobic zone is provided with a water outlet and a biogas outlet anaerobic zone. The utility model multi-zone type bioreactor comprises the sleeve structure's outer cylinder and inner cylinder, said inner cylinder's forming an anaerobic area, said outer cylinder and the inner cylinder to form the aerobic zone and settling zone, so as to improve the anaerobic reaction effect, oxygen supplying ability and strengthening the deposition, improves the water quality, and it has simple structure and is easy to implement.
NOVELTY - This utility model claims one kind of sewage processing biochemical pool, comprising a plurality of orderly connected's biochemical tank, said biochemical baffle plate and baffle plate's groove's longitudinally placed transversely staggered is divided into several independent's biochemical sub-groove, said biochemical groove is provided with a biological nest in said biological nest is provided with a cultured and naturalized biological nest filler, said biochemical slot's more microbial population in turn is provided with a through hole. This utility model adopts multilevel biological groove, and the biological tank is divided into a plurality of sub-groove, and is provided with a biological nest's plurality of microorganisms cultured and naturalized group, improves the sewage processing capability's biochemical pool's in different biological groove, in addition the structure but also saves the floor space.
NOVELTY - Sludge is processed by crushing combustible waste material into granules; mixing with sludge with 70-80% water content in stirring device until water content is reduced to 40-60%; stirring, conveying into extruding machine using conveyor belt, extruding and dehydrating up to 10-15% water content; and forming, storing and transporting.    USE - Method for processing sludge (claimed).
NOVELTY - This utility model claims one kind of biomass and sludge to prepare solid fuel's system, wherein the system comprises a raw material processing system, a forming system and in a boiler system, raw material processing system set on the glass temperature room's first gas input port and the sludge drying crushing device's gas output port through the first gas conveying pipeline connected with the biomass boiler of the steam output port's input port's second gas through the gas conveying pipeline and the sludge drying and crushing device is connected with the smoke output port's biomass boiler through the third gas conveying pipeline and the second gas input chamber's glass; The utility model has the advantages of saving resource, stable operation, is suitable for industrial production on a large scale solid fuel and so on.
NOVELTY - This utility model is one kind of sludge resource utilization device. The utility model is mainly composed of sludge storage pool, high temperature and high pressure reactor, plate-and-frame filter press, drying mixing tank, making the anaerobic reactor, a marsh gas boiler, . Sludge orderly by storage, high temperature high pressure reaction, releasing, dehydrating, drying, stick and so on process, a sludge dewatering filter liquid by anaerobic treatment, anaerobic marsh gas generated by the marsh gas boiler is converted to high pressure steam for the system itself. The utility model compared with the existing technology, the invention has the following advantages: the utility model through scientific design, the sludge into biomass energy, so as to realize the real meaning's up sludge to achieve uniform's economic benefit and environmental benefit, and has low energy consumption, good treatment effect's.
NOVELTY - A biomass semi-coke manufacturing method involves selecting 55-70 wt.% low grade coal, 25-40 wt.% biomass charcoal and 4-8 wt.% adhesive, press-molding mixture, drying 650-800 degrees C for 10-15 hours, and sintering resultant product to obtain finished product.    USE - Method for manufacturing biomass semi-coke.    ADVANTAGE - The method enables manufacturing biomass semi-coke in an inexpensive and eco-friendly manner.
NOVELTY - A methanol gasoline additive contains 85 wt.% methanol, 1 wt.% emulsifier, and 14 wt.% water.    USE - Methanol gasoline additive for fuel in cooking.    ADVANTAGE - The additive has wide raw material source, low cost, simple preparation, high fuel heat value, stable combustion, adjustable flame, and no smoke and carbon, and is easy to control, non-volatile, insoluble in water, safe, reliable, and good for operator's health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol gasoline additive which involves adding ethyl acetate, absolute ethyl alcohol, glycerin, ferrocene, and dimethylbenzene, fully stirring to obtain emulsifier, heating methanol, obtained emulsifier, and water to 280 degrees C in reaction container, and fully stirring.
NOVELTY - A municipal solid waste-derived fuel is prepared by breaking municipal solid waste garbage bags, removing and collecting ferromagnetic material in garbage, crushing remaining garbage to 100-150 mm particle diameter, drying crushed garbage until wastewater content is less than or equal to 10%, secondary-crushing to 30-50 mm, removing and collecting aluminum, sorting light combustible garbage from heavy combustible garbage, uniformly mixing light combustible garbage with calcined lime in which amount of calcined lime is 5-12 wt.% of light combustible garbage, and extruding quicklime light combustible garbage.    USE - Preparation of municipal solid waste-derived fuel (claimed).    ADVANTAGE - The preparation greatly reduces garbage volume, recovers iron and aluminum, treats odor generated in process before discharging in atmosphere, and obtained solid fuel has uniform shape.
NOVELTY - The utility model is as follows: straw biomass raw fuel gas furnace, it uses straw, wheat straw, corn straw, branches and so on or press forming's raw material as fuel, directly into the furnace, one secondary charging can be continuously stable combustion, and tar-free, high thermal efficiency, pure gas, and using are very convenient. It is composed of upper and lower furnace structure's lower furnace body is inner and outer two layers, the heat insulating material is set in the middle, the bottom's lower furnace body is equipped with a wind inlet distribution plate's upper surface is upper furnace body, lower furnace body shell's upper body is inner and outer 3 layers, wherein the inner layer is an insulating layer, inner and outer middle is evenly distributed with 10 isolation plates, comprising upper and lower's curve. The back's upper body is installed with cleaner, side cleaner is equipped with 3's output pipe are respectively connected with heating furnace, stove and water heater.
NOVELTY - The system has a pressure vessel (101) that includes a gas inlet, a gas outlet and a fluid inlet. A compressor introduces the high pressure fluid into the pressure vessel via the fluid inlet so as to compress a volume of gas in the pressure vessel and to absorb soluble gases into the high pressure fluid in the pressure vessel. A flash tank is made to communicate with the pressure vessel for releasing the absorbed gases at ambient pressure from the high pressure fluid.    USE - Gas compression and upgrade system for compressing biogas.    ADVANTAGE - The efficiency of the gas compression system is improved, the capital cost is reduced, very broad spectrum of operational range is covered, and wide range of operating pressure is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas sompression and upgrade system.    Pressure vessels (101,102)    Low pressure gas source (103)    Valves (111,112)    Nozzle (115)    Double walled coil (123)
NOVELTY - Apparatus comprises sequentially arranged on a downstream side and technologically interconnected pulper packets, an iron separator of a first stage, a console crashing inertial separator, a screening surface which consists of a series of cascaded stacked grate cantilever type, that are constricted from the base to the free edge, an eddy current separator of the first stage, a rotary cutter grinder, an iron separator of second stage shock rotary disintegrator equipped with a suction fan, a cyclone separator, an eddy current of second stage, a vibrating screen, and a finished goods warehouse.    USE - The apparatus is useful to produce solid fuel from municipal solid waste, where the solid fuel is useful for producing construction binding materials (claimed).    DETAILED DESCRIPTION - Apparatus comprises sequentially arranged on a downstream side and technologically interconnected pulper packets, an iron separator of a first stage, a console crashing inertial separator, which combines the functions of separation by size and elasticity, a screening surface which consists of a series of cascaded stacked grate cantilever type, that are constricted from the base to the free edge, an eddy current separator of the first stage, a rotary cutter grinder, an iron separator of a second stage shock rotary disintegrator equipped with a suction fan, a cyclone separator, an eddy current of second stage, a vibrating screen, and a finished goods warehouse.
NOVELTY - The reactor has internal sections separated by helical spiral parts. A gas chromatograph is positioned at an outer side of the reactor and analyzes synthesis gases.    USE - Reactor for obtaining gas from biomass or organic residues.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a reactor.
NOVELTY - Transesterification of fatty acid esters, comprises contacting a catalyst comprising at least one of barium oxide or apatite with a reaction medium comprising at least one reactant oil which is vegetable oil and fats.    USE - The method is useful for transesterification of fatty acid esters (claimed) for producing fatty acid glycerin and biodiesel.    ADVANTAGE - The method: provides 100% conversion of fatty acid esters by using catalysts; produces the products with a purity greater than 96.5%; and utilizes the catalysts which are obtained from cheaper raw materials, thus making the method as cost-effective for production on a large scale.
NOVELTY - Fractionating oil seed extraction material, involves establishing an amount of oil seed extraction material in an amount of supercritical carbon dioxide in a first oil seed extraction material separation zone at 60-110 degrees C; adjusting pressure in the separation zone to 200-400 bar to achieve a density of the supercritical fluid of 0.75-0.85 g/ml; and separating a phosphatide fraction from the material in the amount of supercritical carbon dioxide resulting in a triglyceride fraction and a fatty acid fraction remaining in the carbon dioxide.    USE - For fractionating oil seed extraction material to separate phosphatide fraction, triglyceride fraction and fatty acid fraction (claimed) used in production of biodiesel, and as food grade oil.    ADVANTAGE - The method generates at least one oil seed extraction material fraction without utilization of conventional productions steps comprising generation of soap stock and centrifugation.    DETAILED DESCRIPTION - Fractionating oil seed extraction material, involves establishing an amount of oil seed extraction material in an amount of supercritical carbon dioxide in a first oil seed extraction material separation zone at 60-110 degrees C; adjusting pressure of the amount of oil seed extraction material in the amount of supercritical carbon dioxide in the first oil seed extraction material separation zone to 200-400 bar to achieve a density of the supercritical fluid of 0.75-0.85 g/ml; and separating a phosphatide fraction from the oil seed extraction material in the amount of supercritical carbon dioxide resulting in a triglyceride fraction and a fatty acid fraction remaining in the amount of supercritical carbon dioxide.
NOVELTY - Method for preparing biodiesel fuel, involves hydrolyzing the phospholipid in biomass feedstock by processing the biomass feedstock with an enzyme having hydrolysis activity with respect to phospholipid, and performing esterification with the fatty acid to obtain product.    USE - The method is useful for preparing biodiesel fuel (claimed).    ADVANTAGE - The method is simple to perform.
NOVELTY - An electrochemical power system comprises vessel comprising cathode, anode, bipolar plate and reactants containing hydrino reactants during cell operation with separate electron flow and ion mass transport, and electrolysis system. The reactants comprise at least two components chosen from source of water, source of oxygen, source of catalyst or catalyst comprising hydrogen, oxide, oxygen, hydroxide, hydroxyl ion and nascent water, source of atomic hydrogen or atomic hydrogen, and reactants to form source of catalyst, catalyst, source of atomic hydrogen and atomic hydrogen.    USE - Electrochemical power system (claimed).    ADVANTAGE - The electrochemical power system has excellent stability and durability.    DETAILED DESCRIPTION - An electrochemical power system comprises vessel comprising cathode, anode, bipolar plate and reactants containing hydrino reactants during cell operation with separate electron flow and ion mass transport, and electrolysis system. The reactants comprise at least two components chosen from source of water, source of oxygen, source of catalyst or catalyst comprising hydrogen (nH, where n is integer), oxide, oxygen, hydroxide, hydroxyl ion and nascent water, source of atomic hydrogen or atomic hydrogen, one or more reactants to form source of catalyst, catalyst, source of atomic hydrogen, and atomic hydrogen and one or more reactants to initiate the catalysis of atomic hydrogen.
NOVELTY - The method involves stacking fuel cells (10) including a membrane electrode assembly (1). The gas-permeable layers (2,3,5,6) are provided on anode and cathode sides. A separator (7) is provided on one of the anode and cathode sides. A gasket (8) is integrally molded with peripheral edges of the membrane electrode assembly and the gas-permeable layers of stacked fuel cells. A sealing rib (8a) is arranged at one end of the gasket and is configured to be compressed when the module is stacked with fuel cell module (100).    USE - Method for producing fuel cell module.    ADVANTAGE - The sealing rib is arranged at one end of the gasket and is configured to be compressed when the module is stacked with fuel cell module. The adhesion of foreign materials to electrolyte membrane of each fuel cell can be effectively prevented, and highly efficient maintenance can be obtained by replacing fuel cell with degraded performance out of the fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the module having fuel cells and gasket.    Membrane electrode assembly (1)    Gas-permeable layers (2,3,5,6)    Separator (7)    Gasket (8)    Sealing rib (8a)    Fuel cell (10)    Fuel cell module (100)
NOVELTY - Treating lignocellulosic biomass comprises: treating particulate lignocellulosic biomass with alkali to partially remove hemicellulose sheath on cellulose microfibrils of the biomass; and carrying out an oxidation reaction on the alkali treated biomass to form a treated biomass having a disrupted cellulose crystalline structure.    USE - The process is useful for treating lignocellulosic biomass including wood, wood mill waste, begass, agricultural residues, corn stover, cornstalk and perennial grasses (all claimed) to produce biofuel such as bio-ethanol, where the wood includes pine and aspen and the perennial grasses include switchgrass.    ADVANTAGE - The process simply treats the lignocellulosic biomass with reduced energy consumption thus economically producing the ethanol with improved yield in an eco-friendly manner.
NOVELTY - A process of production of biofuel from algae, involves: (a) cultivating a starch-producing algae by autotrophic growth in a first stage; (b) shifting growth from autotrophic growth to heterotrophic growth by inducing stress in the starch-producing algae in a second stage; (c) extracting starch from the starch-producing algae; and (d) utilizing the starch as a component of biofuel production.    USE - For production of biofuel from algae (claimed), such as biodiesel or bioethanol.    ADVANTAGE - The process produces biodiesel, which is atmospherically carbon-neutral, reduces sulfur emissions, produces 20% less carbon monoxide upon use by a consumer, burns more efficiently which results in a smoother-miming engine. The equivalent cetane number of biodiesel is higher than petroleum diesel, reducing diesel noise and knock. Biodiesel produces less soot, reducing particulate emissions by up to 75% and nearly eliminating the black smoke often associated with diesel engine exhausts.
NOVELTY - Device comprises an air separator (7), where the pellets, which are placed in a gas stream, are discharged to fine particles, and an ionization device (4) for at least partially ionizing the gas stream and/or the pellets.    USE - The device is useful for treating pellets, preferably wood pellets (claimed).    ADVANTAGE - The device removes fine particles in pellet fill.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for treating pellets.    Ionization device (4)    Air separator (7)    Screening device (9)    Pivotable flap (10)    Pellet-feed opening (11)
NOVELTY - The method involves heating municipal solid waste in pre-conditioner unit sufficiently to essentially sterilize majority of municipal solid waste. The inorganic materials comprising aluminum and magnetic metals are separated from organic materials comprising cellulosic flakes, wood and textiles. The organic material is exposed to saturated steam environment. The saturated steam environment containing organic matter is heated to temperature of 1600 C and more. A gaseous by-product is produced through heating of organic material in depleted oxygen environment at about 7000 C or more.    USE - Method for treating municipal solid waste in oxygen deprived environment.    ADVANTAGE - The need for manual presorting of garbage can be eliminated. The thousands of tons a day of unprocessed "black bag" garbage or construction debris can be accommodated. The high calorific value fuel used in gas run turbines can be produced to produce electricity and heat. The sizes, quantities and volumes can be scaled or duplicated to provide greater or smaller volumes of processing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolysis unit within waste processing facility.    Autoclave (102)    Fiber (103)    Dryer (104)    Pyrolysis (105)    Gas powered turbine engine (107)
NOVELTY - Hybrid sulfur cycle process comprises: supplying a heat source of substantially 750 degrees C; transferring the heat to a bayonet reactor; establishing a decomposition temperature for sulfuric acid within a catalytic bed housed within the bayonet reactor; maintaining a feed pressure of sulfuric acid within the bayonet reactor at 12 bars; and maintaining a feed pressure of a heat transfer fluid supplied to the bayonet reactor at 15-90 bars.    USE - The hybrid sulfur process is useful for producing hydrogen (claimed).    ADVANTAGE - The process can be operated at lower temperature and pressure ranges while still providing an overall energy efficient cycle process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hybrid sulfur process for hydrogen generation, utilizing the decomposition of sulfuric acid to water, sulfur dioxide and oxygen, comprising: utilizing a sulfur cycle, where an electrolyzer provides sulfuric acid liquid to a sulfuric acid vaporizer reactor operating at 750 degrees C and at a pressure effective to provide vaporized gaseous sulfuric acid and the gaseous sulfuric acid is decomposed to gaseous water, sulfur dioxide and oxygen in a decomposition reactor; passing water, sulfur dioxide and oxygen gases to quench column to capture a sulfuric acid product with additional gases passing to an electrolyzer unit; and inputting electricity to the electrolyzer unit to produce hydrogen gas and a sulfuric acid liquid, where the hybrid sulfur process provides a source for a hydrogen generating process.
NOVELTY - A cellulase derived from intestine of locust, is new. The cellulase has characteristics of (a) substrate containing cellulose is decomposed and reducing sugar is produced, (b) optimum pH of 7, (c) optimum temperature of 50 degrees C, and (d) molecular weight of 50 kDa, 53 kDa, or 30 kDa (based on sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis).    USE - The cellulase is useful in composition and kit for saccharifying cellulose (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microorganisms which live together in intestine of locust, Acrida cinerea or Chilo; (2) composition for saccharification for saccharifying cellulose biomass containing 1 %mass or more of silicons comprising the cellulase or the microorganisms; (3) kit comprising cellulase or microorganisms; (4) antibody coupled with the cellulase; and (5) method for saccharifying cellulose biomass, involves contacting the cellulase, microorganisms or composition with cellulose biomass.
NOVELTY - The method involves supplying biodiesel in a circuit as washing liquid, and making coke oven gas (COG) in contact with the biodiesel in a gas scrubbing stage (3) to separate aromatic hydrocarbons. The biodiesel enriched by the hydrocarbons is withdrawn from the stage, and heated and regenerated by stripping using water vapor. The biodiesel regenerated by stripping is supplied to the stage again after cooling. The COG cleaned in the stage is supplied to another gas scrubbing stage (4) to which a strongly output partial volume of the biodiesel is supplied as washing liquid.    USE - Method for removing aromatic hydrocarbons from COG for benzene, toluene, m-, p-, o-xylene and ethyl benzene laundry.    ADVANTAGE - The method enables reducing concentration of naphthalene in the purified COG less than 50 Milligrams per cubic meter in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for removing aromatic hydrocarbons from COG.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic hydraulic circuit diagram of a device for removing aromatic hydrocarbons from COG with which biodiesel in a circuit is supplied as washing liquid.    Scrubber column (1)    Gas scrubbing stages (3, 4)    Heat exchanger (5)    Regeneration stages (7, 8)    Radiator (9)
NOVELTY - Converting sugarcane and bagasse involves utilizing a carrier, where the carrier is fed with biomass processed with superheated water. A suction pump is provided for processing sludge bagasse. Connectable tubes are connected to the suction pump. Perforated screen is provided where the screen has 400-600 mesh size. A recycle cooler is provided for performing the cooling and concentration of the liquor. The suction pump receives sludge from lignocellulosic material carrier.    USE - Method for converting sugarcane and bagasse (claimed).    ADVANTAGE - The method enables to convert sugarcane and bagasse simultaneously and rapidly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for converting sugar and bagasse.
NOVELTY - Producing ethanol involves processing by-products or biomass obtained during processing Eucalyptus by acid and alkaline pretreatment and enzymatic hydrolysis by using cellulases.    USE - Method for producing ethanol (claimed).    ADVANTAGE - The method enables to produce ethanol by simultaneous saccharification and fermentation process.
NOVELTY - The container has main portion (1) that is provided with the air layer (2c) for heat insulation between an outer peripheral wall (2a) formed in the shape of transparence and inner peripheral wall (2b) formed in the shape of an opaqueness. A ventilation unit (8) changes the air in main portion to the upper surface of cover (5) by ejecting heat energy of sunlight. A valve element opens and closes the ventilating opening (9) which are formed with movement apparatus (11) of valve element (10). The shape memory alloy material (12) is formed in the upper surface of a cover.    USE - Container for processing organic-refuse such as weeds, pruned branch generated from kitchen.    ADVANTAGE - The organic-refuse processing container can prevent the raise of temperature rapidly at the stage of summer from spring, when the air temperature is high. The falling of temperature at the cold stage can be prevented and amount reduction of organic refuse with few moisture contents such as weeds and a branch are achieved effectively with reliable operation.    DETAILED DESCRIPTION - The movement apparatus is provided with the shape memory alloy material which transforms with the heat energy of sunlight and operates a valve element. The ventilating opening is formed in the surroundings of the case (13) accommodated in shape memory alloy material. The valve element is provided in the lower end of the core which vertically moves with the expansion-contraction of coil spring.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the organic-refuse processing container.    Main portion (1)    Outer peripheral wall (2a)    Inner peripheral wall (2b)    Air layer (2c)    Cover (5)    Ventilation unit (8)    Ventilation opening (9)    Valve element (10)    Movement apparatus (11)    Shape memory alloy material (12)    Case (13)
NOVELTY - Fast-growing plant cultivation and composting comprises planting and/or cultivating fast-growing plants in selected land or water area; harvesting when the plants grow to proper height; naturally drying harvested plants; processing dried plants into carbon material; forming plant storage section for sequestering carbon; and processing fast-growing plants or carbon material into organic fertilizer, and processing nitrogen-containing gases produced during composting into nitrogenous fertilizer (ammonia).    USE - Method for fast-growing plant cultivation and composting used for fertilizer production (claimed).    ADVANTAGE - The method realizes negative growth of atmospheric greenhouse gases and regulates greenhouse effect, inhibits haze formation, solves related environmental problems, improves soil structure, and increases soil fertility.
NOVELTY - An olmesartan medoxomil is prepared by preparing 1-(((27-(triphenylmethyl)-2H-tetrazole-5-yl)biphenyl-4-yl)methyl)-2-propyl-4-(1-hydroxy-1-methylethyl)imidazole-5-carboxylic acid(5-methyl-2-oxo-1,3 dioxolen-4-yl)methyl ester, removing fatty acid methyl ester to obtain trityl olmesartan medoxomil, and placing 4-(1-hydroxy-1-methylethyl)-2-propyl-imidazole-5-carboxylate and N-(triphenylmethyl)-5-(4'-bromomethylbiphenyl-2-yl-)tetrazole in solvent under alkaline condition.    USE - Preparation of olmesartan medoxomil (claimed).    ADVANTAGE - Preparation process is simple and low cost and has high yield, mild reaction condition, and less by-product, and product is safe and environment-friendly and has high purity and total yield.    DETAILED DESCRIPTION - An olmesartan medoxomil is prepared by preparing 1-(((27-(triphenylmethyl)-2H-tetrazole-5-yl)biphenyl-4-yl)methyl)-2-propyl-4-(1-hydroxy-1-methylethyl)imidazole-5-carboxylic acid(5-methyl-2-oxo-1,3 dioxolen-4-yl)methyl ester, removing fatty acid methyl ester to obtain trityl olmesartan medoxomil, placing 4-(1-hydroxy-1-methylethyl)-2-propyl-imidazole-5-carboxylate and N-(triphenylmethyl)-5-(4'-bromomethylbiphenyl-2-yl-)tetrazole in solvent under alkaline condition to obtain compound containing 4-(1-hydroxy-1-methylethyl)-2-propyl-1-(4-(2-(trityltetrazol-5-yl) benzylphenyl) phenyl) methyl-5-carboxylate as reaction solution, adding sodium hydroxide into reaction solution to obtain compound 4-(1-hydroxy-1-methylethyl)-2-propyl-1-(4-(2-(trityltetrazol-5-yl) benzylphenyl) phenyl) methyl-5-carboxylate sodium salt as reaction solution, adding cesium carbonate and 4-chloro-1,3-dioxolan-2-one into reaction solution, and reacting.
NOVELTY - Manufacture of hydrocarbon involves mixing (100) aliphatic-containing biomass and coal, and subjecting the obtained feedstock to hydrous pyrolysis, and separating (104) bio-oil from the obtained reaction mixture.    USE - Manufacture of hydrocarbon used for refining process.    ADVANTAGE - The method enables manufacture of hydrocarbon with high conversion and energy efficiency with reduced mass transfer resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for feedstock, which comprises mixture of aliphatic-containing biomass and aliphatic-containing coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating manufacture of hydrocarbon.    Mixing of biomass and coal (100)    Conversion process (102)    Bio-oil separating process (104)    Bio-oil refining process (106)
NOVELTY - Microbial preparation for lipolysis comprises Burkholderia multivorans which has lipolysis ability at 40 degrees C and pH of 4.    USE - The microbial preparation for lipolysis is useful for processing waste liquid (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste-liquid processing method.
NOVELTY - Biochemical reaction system comprises polysaccharide.    USE - The biochemical reaction system is useful for simultaneously producing bio-hydrogen and generating electric power (claimed).    DETAILED DESCRIPTION - Biochemical reaction system comprises polysaccharide, where glucan chain is shortened by phosphorylase, phosphoric acid is taken in and it is set as glucose, and phosphoric acid, hydrogen gas is generated with NADP and water through glucose, by phosphoglucomutase. The part or all of NADPH is generated and dissociated to NADPH, electron (e-), and proton (H+) with coenzyme oxidase, NADPH+ transmits positron permeable film, anode is gathered and electron (e-) is isolated with positron permeable film, cathode is gathered and electron (e-) of cathode moves to the direction of NADPH+ which gathered to the anode, by flowing into a cathode from an anode, and electric current comprises an electric circuit.
NOVELTY - A reaction time shortening structure of biodiesel production device, has biodiesel production device including raw material storage tank, reaction bath for reacting raw material transferred from raw material storage tank, and finished product storage tank for maintaining biodiesel produced from reaction bath. The reaction bath has raw material heating tank with circulation line and transfer line. Vegetable material is processed in raw material heating tank of the reaction bath.    USE - Reaction time shortening structure of biodiesel production device (claimed).    ADVANTAGE - The biodiesel is efficiently produced in short time using the structure with reduced energy consumption.    DETAILED DESCRIPTION - A reaction time shortening structure of biodiesel production device, has biodiesel production device including raw material storage tank, reaction bath for reacting raw material transferred from raw material storage tank, and finished product storage tank for maintaining biodiesel produced from reaction bath. The reaction bath has raw material heating tank with circulation line and transfer line. The volume of transfer line is same as volume of circulation line. Vegetable material is processed in raw material heating tank of the reaction bath. In the reaction bath, washing process using water and drying process are carried out. Vapor heated by steam boiler is supplied to circulation line of reaction bath. Vapor collected through circulation line and transfer line of reaction bath is supplied to circulation line of raw material heating tank.
NOVELTY - Photochemically breaking down carbon dioxide (CO2) involves irradiating a stream of gases with UV light with wavelength of less than 200 nm.    USE - The method is useful for photochemically breaking down CO2 (claimed).    ADVANTAGE - The direct photochemical excitation of CO2 with photons of appropriate energy can cause rupture of the CO bond of CO2 resulting with complete selectivity to CO and that this breakdown may be increased when the process is carried out in the presence of a solid.
NOVELTY - Method of improving speed of anaerobic digestion involves administering microalgae to wastewater sludge digestion tank for anaerobic digestion during which nutrient of microalgae is used for anaerobic digestion and gasification process.    USE - Method of improving speed of anaerobic digestion during production of gas (all claimed) e.g. biogas.    ADVANTAGE - The reliability of digestion tank in which anaerobic digestion is carried out is improved. The biogas is efficiently produced by anaerobic digestion , with improved productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for increasing production of gas;    (2) anaerobic co-digestion process; and    (3) anaerobic co-digestion process reactor.
NOVELTY - Increasing a lipid content of algae, comprises combining algae and a lipid-precipitating addition in a growth-inhibitive medium that is deficient in at least one nutrient which is necessary for reproductive growth of algae, thus frustrating algae reproduction. The lipid-precipitating addition comprises hydroxy-containing compounds or amine-containing compounds.    USE - The method is useful for increasing the lipid content of algae, where the lipid is useful for producing methyl ester (claimed) that is useful as biodiesel.    ADVANTAGE - The method: provides the methyl ester which can be directly used as biodiesel without any transesterification or esterification; does not form the lipid in dissolved form, which is toxic to organisms; improves the productivity and product yield of lipid; reduces the cost of downstream lipid collection and separation; and provides faster formation of lipid particles/droplets from organic materials.
NOVELTY - Producing hydrocarbon and hydrogen fuels comprises (a) fermenting a biomass material containing fermentation medium with an inoculum comprising a mixed culture of microorganisms derived from the rumen contents of a rumen-containing animal and incubating under anaerobic conditions and for a sufficient time to produce volatile fatty acids in the medium, and (b) subjecting the volatile fatty acids or their salts to electrolysis under conditions effective to convert the volatile fatty acids or their salts to hydrocarbons and hydrogen.    USE - The method is useful for producing hydrocarbon and hydrogen fuels (claimed) such as ethanol for motor vehicle and gasoline-powered vehicle.    ADVANTAGE - The method rapidly, flexibly and efficiently produces hydrocarbon and hydrogen fuels with high yield by utilizing carbon dioxide as fuel-producing feedstock and without high temperatures or high energy requirements and need for landfilling of the biomass waste, thus reducing production cost of the hydrocarbon and fuels.    DETAILED DESCRIPTION - Producing hydrocarbon and hydrogen fuels comprises (a) fermenting a biomass material containing fermentation medium with an inoculum comprising a mixed culture of microorganisms derived from the rumen contents of a rumen-containing animal and incubating under anaerobic conditions and for a sufficient time to produce volatile fatty acids in the medium, and (b) subjecting the volatile fatty acids or their salts to electrolysis under conditions effective to convert the volatile fatty acids or their salts to hydrocarbons and hydrogen, and further comprises concentrating the volatile fatty acids by distillation, filtration or capacitive deionization in the medium prior to the electrolysis.
NOVELTY - Biogas plant comprises a first reactor (2) and a second reactor (3). A substrate is supplied into the first reactor. The substrate is passed from the first reactor to the second reactor. The first reactor is arranged in the second reactor. The substrate, which is withdrawn from the first reactor, is passed through a separator (8) and is fed back to the first reactor.    USE - Used as the biogas plant.    ADVANTAGE - The biogas plant maintains a high concentration of microorganisms and removes foreign substances from the substrate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Biogas plant (1)    First reactor (2)    Second reactor (3)    Gas collecting chamber (5)    Separator (8)
NOVELTY - An ethanol from lignocellulose raw material is manufactured by using sprouting germinated from stump after cutting down woody plant as lignocellulose raw material.    USE - Manufacture of ethanol from lignocellulose raw material (claimed).    ADVANTAGE - The method efficiently manufactures ethanol from sprouting of woody plant.
NOVELTY - Ethanol is manufactured from saccharide of herbal biomass or wood biomass by treating herbal biomass or wood biomass with alkaline solution, separating alkali-treated solution into alkaline solution and solid component, replenishing separated alkaline solution with alkali substance, and using replenished alkaline solution in alkali treatment process.    USE - Manufacture of ethanol from saccharide of herbal biomass or wood biomass for fuel.    ADVANTAGE - Ethanol can be manufactured at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the manufacturing method of ethanol from saccharide of herbal biomass or wood biomass. (Drawing includes non-English language text).    Alkali treatment tank (1)    1st solid-liquid separator (2)    1st recycle pipe (3)    Alkali replenishment part (4)    2nd solid-liquid separator (6)
NOVELTY - The method involves reducing content of ammonia nitrogen contained in digestive liquid (11) and performing methane-fermentation of organic waste (10) on anaerobic conditions. The aerobic process of the residual organic substance which remained in the digestive liquid without decomposed at the process of ammonia nitrogen and methane fermentation is performed by aerobic denitrifying bacteria as a main nutrient.    USE - Method for processing nitrogen component contained in methane fermentation digestive liquid.    ADVANTAGE - Since the metabolic activity of the aerobic denitrifying bacteria can be improved, the reduction efficiency of the ammonia nitrogen in the digestive liquid can be improved. The installation cost of the nitrogen processing apparatus is reduced and the efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for processing nitrogen component contained in methane fermentation digestive liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of nitrogen processing apparatus. (Drawing includes non-English language text)    Methane fermentation tank (2)    Ammonia-nitrogen reduction tank (3)    Storage tank (4)    Organic waste (10)    Digestive liquid (11)
NOVELTY - Method for processing organic waste liquid involves carrying out anaerobic fermentation process of organic waste liquid, generating digestive liquid containing ammonia nitrogen, adding chemical oxygen demand (COD) component to digestive liquid, performing gas-liquid contact of digestive liquid, carrying out assimilation and/or biological aerobic treatment, diffusing gaseous nitrogen, denitrifying ammonia nitrogen in digestive liquid.    USE - Method for processing organic waste liquid (claimed).    ADVANTAGE - The method enables efficient processing of organic waste liquid, by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of organic waste liquid.
NOVELTY - Anaerobic-biological-treatment method involves methane-fermenting wastewater containing organic substance under anaerobic, and performing anaerobic biological treatment at water temperature of less than 35 degrees C in presence of gel-like carrier (16).    USE - Anaerobic-biological-treatment method (claimed).    ADVANTAGE - The method stably treats wastewater discharged from electronic industrial factory, pulp manufacturing plant, chemical plant, and granule sludge dissect and refines.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-biological-treatment apparatus (1).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic-biological-treatment apparatus for treating wastewater. (Drawing includes non-English language text)    Anaerobic-biological-treatment apparatus (1)    Anaerobic reaction tank (10)    Draft tube (12)    Stirring apparatus (14)    Gel-like carrier (16)
NOVELTY - The organic-refuse disposal machine (5) has processing tank (6) into which crushed organic refuse is introduced. A stirring shaft (9) is mounted with stirring blades (8). A decomposing water processing tank (13) is provided with waste water sterilization agent (14). A liquid pure enzyme group is filled in decomposition process material tank (18) to help decomposition-disposal and fat splitting process of organic refuse. The water supply to the processing tank is stopped when porous filtration drain wall (12) is clogged.    USE - Sink cabinet built-in disposal machine for organic-refuse e.g. cooking waste, meal residue or fish intestine, raw big root vegetable, fish bone, eggshell and foot bones of hen, installed in kitchen.    ADVANTAGE - The odor generation from the organic-refuse is prevented. The mental embarrassment of the house wife is prevented. The rubbish disposal labor is not needed. The waste material disposal cost and running cost of the disposal machine can be reduced. The eradication process within decomposition process tank is made easy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sink cabinet built-in organic-refuse disposal machine. (Drawing includes non-English language text)    Organic-refuse disposal machine (5)    Processing tank (6)    Stirring blade (8)    Stirring shaft (9)    Porous filtration drain wall (12)    Decomposing water processing tank (13)    Waste water sterilization agent (14)    Decomposition process material tank (18)
NOVELTY - A thermal support tunnel machine complex comprises a hot-gas passage, a tunnel wall, a waste chamber, a roof, a roof cover, a support frame, a water receiving tray, a rail, a cover wall, a lateral wall, an upper bottom part, a lower bottom part, a hot-gas passage gate, a waste inlet, a waste outlet, a smoke guide hole partition wall, a windproof gate, a thermal access hole, and an exhaust gas outlet.    USE - Thermal support tunnel machine complex used in biological composting of organic wastes.
NOVELTY - Alcohol production involves applying an electric field for fermenting sugar broth. The fermentation of sugar broth is performed by preparing a container for raw broth containing two electrodes, where the electrodes are connected to the source of direct current. The broth is prepared for fermentation, where the container is filled in batches or continuously. The electrodes are connected to the sugar molecules.    USE - Method for producing alcohol used as a chemical solvent and automotive fuel.    ADVANTAGE - The method produces alcohol with improved yield by fermentation of sugars in a simple and cost-effective manner.
NOVELTY - The apparatus (100) has a generation unit (111) that generates the fermentation product. A vacuum unit (110B) is connected with the generation unit. A decompression device is provided to supply a vaporization fermentation product to a porous membrane while vaporizing the fermentation product for generating the vaporization fermentation product. The periphery of porous membrane is cooled by a cooling unit. A collection unit is provided to collect vaporization fermentation product from the porous membrane.    USE - Fermentation concentration apparatus used for concentrating and generating fermentation product e.g. bioethanol used as fuel.    ADVANTAGE - The fermentation product can be concentrated efficiently. The fermentation product can be generated effectively. The by-products can be removed continuously from generation unit. The generation of fermentation product can be stimulated in fermentation concentration apparatus. The boiling point of fermentation product can be reduced. The requirement for heating generation unit normally in fermentation concentration apparatus can be prevented. The concentration of fermentation product in generation unit can be maintained lesser than deactivation concentration. The transmission rate of fermentation product can be improved.    DETAILED DESCRIPTION - The apparatus has a generation unit that is connected to the porous membrane. The fermentation operation and concentration operation for fermentation product are performed simultaneously. An INDEPENDENT CLAIM is included for a fermentation concentration method for concentrating and generating fermentation product.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fermentation concentration apparatus.    Fermentation concentration apparatus (100)    Fermentation apparatus (110A)    Vacuum unit (110B)    Generation unit (111)
NOVELTY - Apparatus (1) comprises a manure fermentor (2), which has an outer peripheral wall of predetermined height, where a roof material (8) is arranged on the outer peripheral wall. A crane is provided to regulate up-and-down motion of the roof material, where spacing is adjusted between the roof material and the outer peripheral wall.    USE - Apparatus used for producing an organic manure from animal excrements, including hen droppings, cattle feces, and pig feces, foodstuff residue, and coppiced timber (claimed).    ADVANTAGE - The apparatus converts water into hot water efficiently, prevents production of malodor from manure, and secures easy air conditioning and high carrying capacity of manure.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an apparatus.    Apparatus (1)    Manure fermentor (2)    Front door (4)    Right-and-left side wall (5)    Roof material (8)
NOVELTY - Composting method of timber involves swelling and softening wood chips (3) to produce processed chip (5), reducing temperature to 30 degrees C or more and less than 100 degrees C, adding nutrition material for improving the microorganisms activity of microbial cell, which understands the processed chip by microorganisms, mixing to produce composting chip (6), and curing.    USE - Composting method of timber used for slope revegetation (claimed).    ADVANTAGE - The recycling of plant material is efficiently enabled.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composting system of timber, which has processing apparatus (4) for swelling and softening wood chips, temperature reduction unit for reducing the temperature of processed chip, and curing unit;    (2) slope revegetation method, which involves stirring and mixing compost produced by the composting method with another growth material, producing growth material slurry, and spraying slurry on a slope face; and    (3) slope revegetation system (31), which has the timber composting system and spraying machine (33) having spray hose (34) and nozzle (35).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of slope revegetation system. (Drawing includes non-English language text)    Wood chip (3)    Processing apparatus (4)    Processed chip (5)    Composting chip (6)    Revegetation system (31)    Slope face (32)    Spraying machine (33)    Hose (34)    Nozzle (35)
NOVELTY - Recombinant polypeptide comprising an amino acid sequence having at least 97% or 98% sequence identity to amino acids 2-377 of SEQ ID NO:78 (a 447 amino acid sequence fully defined in the specification), is new.    USE - The recombinant polypeptide is useful in a recombinant cell, which is useful for producing xylose isomerases used to convert xylose to xylulose for biofuels production.    ADVANTAGE - The recombinant polypeptides provide xylose isomerases with improved tolerance to acidic conditions and enhanced activity to convert xylose to xylulose.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a polypeptide comprising an amino acid sequence having a nucleotide sequence having at least 70%, at least 75%, at least 80%, at least 85%, at least 90%, at least 93%, at least 95%, at least 96%, at least 98%, at least 99%, at least 100% sequence identity, to SEQ ID NOs: 2-176 (one of 88 (442-449) amino acid sequences all fully defined in the specification) (only even numbers), or to a catalytic or dimerization domain;    (2) a nucleic acid which encodes a polypeptide;    (3) a vector comprising the nucleic acid;    (4) a recombinant cell engineered to express the polypeptide;    (5) a host cell transformed with the vector; and    (6) producing a fermentation product comprising culturing the recombinant cell in medium containing xylose under conditions in which the fermentation product is expressed.
NOVELTY - Concentrating biofuels that relies on phase separation and on the progressive freezing of water from organic broths containing alcohols, fatty acids or lipids in aqueous solutions, is claimed.    USE - The method is useful for concentrating biofuels (claimed), and removing a substantial fraction of water from the products of fermentation or photosynthetic algae.    ADVANTAGE - The method is capable of simply and economically concentrating the biofuels using phase change techniques with high efficiency and reduced energy consumption in batch or continuous mode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for concentrating biofuels.
NOVELTY - Biogas plant comprises a fermenter tank (1), an aggregate carrier (2), which is mounted in a vertically aligned manner in the fermenter tank, and a aggregate (10), preferably a submersible motorized stirring device, which is mounted height adjustably at the aggregate carrier using a height adjustment device (11). The height adjustment device is formed by a belt drive. A traction means of the belt drive is led by at least two deflecting elements (15, 38), which is spaced in aggregate carrier-longitudinal direction. At least one deflecting elements is rotatably driven using a drive means.    USE - Used as a biogas plant.    ADVANTAGE - The biogas plant adjusts the aggregate along the aggregate carrier in the fermenter tank in a simple manner over a prolonged period.    DETAILED DESCRIPTION - Biogas plant comprises a fermenter tank (1), an aggregate carrier (2), which is mounted in a vertically aligned manner in the fermenter tank, and a aggregate (10), preferably a submersible motorized stirring device, which is mounted height adjustably at the aggregate carrier using a height adjustment device (11). The height adjustment device is formed by a belt drive. A traction means of the belt drive is led by at least two deflecting elements (15, 38), which is spaced in aggregate carrier-longitudinal direction. At least one of the deflecting elements is rotatably driven using a drive means. The aggregate is coupled with the traction means during a rotational operation. The deflecting element is raised in a first direction and lowered to a second, opposite direction during the rotational operation.    DESCRIPTION OF DRAWING(S) - The figure shows a partial schematic view of the fermenter tank of the biogas plant.    Fermenter tank (1)    Aggregate carrier (2)    Aggregate (10)    Height adjustment device (11)    Deflecting element (15, 38)
NOVELTY - Method for preparing ethanol using lignocellulosic raw material involves performing primary saccharification fermentation of lignocellulosic raw material using hexose fermentative microorganisms, performing secondary fermentation on the liquid obtained by the primary saccharification fermentation using pentose fermentative microorganisms, where the glucose level of the liquid during secondary fermentation is maintained by supplying liquid to the supply port of a secondary fermentation tank which is used during secondary fermentation process.    USE - The method is useful for preparing ethanol using lignocellulosic raw material (claimed).    ADVANTAGE - The method enables to prepare ethanol with high yield.    DETAILED DESCRIPTION - Method for preparing ethanol using lignocellulosic raw material involves performing primary saccharification fermentation of lignocellulosic raw material using hexose fermentative microorganisms, performing secondary fermentation on the liquid obtained by the primary saccharification fermentation using pentose fermentative microorganisms, where the glucose level of the liquid during secondary fermentation is maintained by supplying liquid to the supply port of a secondary fermentation tank which is used during secondary fermentation process, and the glucose level of the liquid is maintained to 0.5 %mass. The primary saccharification fermentation process is performed by residence time so that the glucose level of the culture solution discharged from the discharge port of the primary saccharification fermenter used by the primary saccharification fermentation process is 1 %mass or less.
NOVELTY - Invention relates to installation for production of alcohol and accompanying materials, which contains source of thermal energy, connected to fermentation vat with prepared biomass, to wash distillation aggregate with distillation column, connected with circulation pump. Installation is characterised by the fact that source of thermal energy is made in form of two separate sources of low-potential and high-potential energy, and as low-potential source, connected via newly introduced heat accumulator to fermentation vat, used are successively connected flat solar collectors and vacuum-tube collectors, and high-potential source contains newly introduced solar concentrator, in focus of which placed is heat-exchanger with high-temperature working body, connected to additional heat accumulator, connected with wash distillation aggregate and with distillation column.    USE - Chemistry.    ADVANTAGE - Power installation for production of alcohol and accompanying materials is energy independent and can be used autonomously, including in dark part of the day, on remote territories, provided with required raw material for fermentation.1 dwg
NOVELTY - Wastewater flows in a regulation pool, a hydrolysis acidification pool, an aerobic pool (p1), a preliminary sedimentation pool, a facultative pool, an aerobic pool (a2) and a secondary sedimentation pool, and is finally discharged after meeting standard requirements. In addition, the hydrolysis acidification pool, the aerobic pool (a1), the facultative pool and the aerobic pool (a2) are respectively added with 1-2.5% microbial carriers and 1.5-4% environmental microorganism preparations based on their respective volumes.    USE - Method for removing total nitrogen during treatment of coking wastewater (claimed).    DETAILED DESCRIPTION - Wastewater flows in a regulation pool, a hydrolysis acidification pool, an aerobic pool (p1), a preliminary sedimentation pool, a facultative pool, an aerobic pool (a2) and a secondary sedimentation pool, and is finally discharged after meeting standard requirements. The hydrolysis acidification pool, aerobic pool (a1) and the preliminary sedimentation pool form first-stage A/O system. The facultative pool, aerobic pool (a2) and secondary sedimentation pool form second-stage A/O system. The first-stage and second-stage A/O systems form two independent sludge systems. In addition, the hydrolysis acidification pool, the aerobic pool (a1), the facultative pool and the aerobic pool (a2) are respectively added with 1-2.5% microbial carriers and 1.5-4% environmental microorganism preparations based on their respective volumes.
NOVELTY - Synthesis of N-(phosphonomethyl)glycine (glyphosate) or one of its derivatives selected from its salts, its phosphonate esters and its phosphonate ester salts, involves: a) forming a reaction mixture comprising acid catalyst, N,N'-bis(carboxymethyl)-2,5-diketopiperazine and a compound comprising P-O-P anhydride moieties, to form N,N'-bis(phosphonomethyl-2,5-diketopiperazine, its dehydrated forms or their phosphonate esters; and b) hydrolyzing the mixture to form N-(phosphonomethyl)glycine or its derivatives selected from its salts, its phosphonate esters and its phosphonate ester salts.    USE - For synthesis of N-(phosphonomethyl)glycine (claimed), useful in controlling the growth of germinating seeds, emerging seedlings, maturing and established woody and herbaceous vegetation, and aquatic plants; used as a systemic post-emergent herbicide to control the growth of a wide variety of annual and perennial grass and broad leaf weed species in cultivated crop lands, including cotton production; and used in aqueous herbicidal formulations.    ADVANTAGE - The method is an economical and environmental friendly method for the manufacture of N-(phosphonomethyl)glycine or one of its derivatives.    DETAILED DESCRIPTION - Synthesis of N-(phosphonomethyl)glycine or one of its derivatives selected from its salts, its phosphonate esters and its phosphonate ester salts, involves a) forming a reaction mixture comprising an acid catalyst, N,N'-bis(carboxymethyl)-2,5-diketopiperazine and a compound comprising P-O-P anhydride moieties, where moieties comprise one P atom at oxidation state (+3) and the other P atom at the oxidation state (+5) or (+5), to form N,N'-bis(phosphonomethyl-2,5-diketopiperazine, its dehydrated forms or their phosphonate esters; b) hydrolyzing the reaction mixture to form N-(phosphonomethyl)glycine or its derivatives selected from its salts, its phosphonate esters and its phosphonate ester salts.
NOVELTY - Preparing graphite alkenyl solid alkali catalyst involves utilizing oxidized graphite alkene as a carrier and potassium sodium tartrate as the load, where oxidized graphite alkene is obtained through Hummers method. Potassium sodium tartrate is obtained by using roasting.    USE - Method for preparing graphite alkenyl solid alkali catalyst used for production of biodiesel, soybean oil, rapeseed oil, palm oil and vegetable oil (claimed).    ADVANTAGE - The method enables to prepare graphite alkenyl solid alkali catalyst in a simple, eco-friendly, efficient and cost-effective manner.
NOVELTY - Soil peanut special slow release fertilizer comprises urea, ferrous sulfate, potassium sulfate, potassium dihydrogen phosphate, copper sulfate, calcium superphosphate, fermented livestock and poultry manure, sulfur, and sodium silicate, where the fermented livestock and poultry manure is prepared by uniformly mixing chicken manure, sheep manure, and dairy manure, and adding to crushed straw and fermentation agent, performing fermentation, and drying, and crushing the obtained product.    USE - As soil peanut special slow release fertilizer.    ADVANTAGE - The soil peanut special slow release fertilizer enables to improve nutrient content of the soil, utilization ratio of fertilizer, and peanut yield and quality, and is environmentally-friendly.    DETAILED DESCRIPTION - Soil peanut special slow release fertilizer comprises 10-20 pts. wt. urea, 5-10 pts. wt. ferrous sulfate, 5-10 pts. wt. potassium sulfate, 5-10 pts. wt. potassium dihydrogen phosphate, 2-5 pts. wt. copper sulfate, 15-25 pts. wt. calcium superphosphate, 7-19 pts. wt. fermented livestock and poultry manure, 3 pts. wt. sulfur, and 2 pts. wt. sodium silicate, where the fermented livestock and poultry manure is prepared by uniformly mixing 2-5 pts. wt. chicken manure, 2-5 pts. wt. sheep manure, and 2-5 pts. wt. dairy manure, adding manure mixture to crushed straw with length of 5-8 cm in a ratio of 2:8, stacking and adding 0.2% fermentation agent, where the width of the stack is 1.5-2 m, and the height of the layer in the stack is 20-25 cm, adding water to the mixture, until the water content is 50-60%, raising the temperature to more than 60 degrees C, performing fermentation, and drying, and crushing the obtained product, where the fermentation agent (per ml) comprises 1-1.5x 109 Streptococcus thermophilus, 0.3-0.5x 108 IU neutral protease, 0.1-0.2x 106 IU cellulase, 3-4 x 105 IU triacylglyceride diacylglycerol, 1-2x 105 IU beer yeast, and 3-4x 106 IU Bacillus subtilis.
NOVELTY - L-praziquantel is prepared by mixing 1,2,3,6,7,11 beta -hexahydro-4H-pyrazino(2,1- alpha )isoquinoline-4-one phosphate compound and base, dissolving in solvent, reacting, dehydrating, adding L-tartaric acid resolving agent, heating to dissolve, cooling to crystallize, dissolving in solvent, recrystallizing, carrying out hydroformylation with chlorocyclohexane in cyclohexanone under basic conditions, adding organic solvent, decolorizing with activated carbon, washing, recrystallizing to refine, filtering, and vacuum drying.    USE - Method for preparing L-praziquantel (claimed).    ADVANTAGE - The process is short, selective, high in yield and environment-friendly. The compound has excellent quality.
NOVELTY - A composting garbage bag comprises compostable biological-based resin and garbage bag body.    USE - Composting garbage bag used for household garbage and compost.    ADVANTAGE - The composting bag can lower energy required waste incineration and reduce pollution caused by burning.
NOVELTY - A cultivating composition comprises corn cob powder, wheat bran, soybean powder, corn powder, gypsum powder, and selenium salt.    USE - A cultivating composition used for mushroom (claimed).
NOVELTY - Preparation of a grain straw sawdust comprises crushing straw particles to wood chips, and mixing with auxiliary material.    USE - Method for the preparation of a grain straw sawdust used for cultivating black fungus (claimed).    ADVANTAGE - The grain straw sawdust achieves good quality and high yield black fungus.
NOVELTY - Manufacturing substituted 3-fluoromethyl-pyrazolidine-4-carboxylic acid compounds (I), involves submitting substituted 3-fluoromethyl-pyrazolidine-4-carboxylic acid compounds (II) to a reduction reaction in the presence of an ammonium salt (III).    USE - The process is useful for preparing (I), which is useful for manufacturing an agrochemically or pharmaceutically active compound (claimed), preferably pyrazole carboxanilide fungicides, where (I) is esters of 3-difluoromethyl-1-methyl-1H-pyrazole-4-carboxylic acid. No biological data given.    ADVANTAGE - The process allows for a high selectivity with low degrees of over-reduction, high efficiency, such as yield of the desired products, and an easier work-up, and is an environmentally or economically beneficial process.    DETAILED DESCRIPTION - Manufacturing substituted 3-fluoromethyl-pyrazolidine-4-carboxylic acid compounds of formula (I), involves submitting substituted 3-fluoromethyl-pyrazolidine-4-carboxylic acid compounds of formula (II) to a reduction reaction in the presence of an ammonium salt of formula (Z-N+R3R4R5R6) (III).    Y1 = H, F, alkyl, cycloalkyl, aralkyl or aryl;    R1, R2, R1a, R2a = H or organic residue; and    X = Cl, Br, I, CN, sulfate or sulfonate;    Z- = anion; and    R3-R6 = H, alkyl, aralkyl or aryl, provided that R3-R6 are not all H.    An INDEPENDENT CLAIM is included for manufacturing an agrochemically or pharmaceutically active compound, comprising (a) manufacturing (I) which comprises submitting (II) to a reduction reaction, and (b) submitting the crude product mixture obtained in step (a) to a subsequent synthetic step, where no purification step of the crude product mixture is performed between step (a) and step (b).
NOVELTY - A plant cultivation composition comprises algae digestate; and organic carbon.    USE - As plant cultivation composition (claimed) useful for generating soil regenerating products and other agricultural applications.    ADVANTAGE - The composition reduces seedling development time by at least 10%, at least 20%, and at least 30%; increases messenger ribonucleic acids (mRNA) content in plant cells; and increases content of at least one plant enzyme selected from catalases, peroxidases, diphenoloxidases, and invertases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) making (M1) plant cultivation composition involving digesting algae in an anaerobic bioreactor to produce digestate solids and digestate liquor; pyrolyzing biomass to produce pyrolyzed biomass including organic carbon; and combining the pyrolyzed biomass with at least one of the digestate solids and the digestate liquor;    (2) method (M2) for using plant cultivation composition involving acquiring the plant cultivation composition; and applying the plant cultivation composition to soil and/or plants.
NOVELTY - Preparation of urea ammonium nitrate solution comprises placing 65-78% urea in stainless steel container at 85-95 degrees C and 0.4 MPa and standing; placing 85-97% ammonium nitrate in stainless steel container at 130-135 degrees C and 1.6 MPa and standing; and stirring, adding 5 kg water, reducing pressure at 0.4 MPa, adding 12-15 kg ammonium nitrate solution into container, stirring, adding 16-19 kg urea solution, continuously stirring, and reacting for 1-2 hours.    USE - Method for preparing urea ammonium nitrate solution (claimed).    ADVANTAGE - The method is energy-saving and environment-friendly, and has flexible operation, low consumption and low production cost.
NOVELTY - A low-carbon composite biological organic silicon-magnesium-potassium fertilizer comprises 60-70 wt.% silicon-based organic material, 5-10 wt.% magnesium sulfate, 10-15 wt.% calcium superphosphate, and 10-15 wt.% potassium sulfate. The silicon-based organic material is prepared by drying 70 wt.% oil shale at 100 degrees C for 5-10 hours, milling into 100-200 mesh to obtain powder, putting in fermentation tank, adding 14 wt.% straw powder, 10-20 wt.% medical stone powder or zeolite powder, 5 wt.% wheat bran, 0.6 wt.% yeast and 0.4 wt.% urea, fermenting at 50-70 degrees C for 7-8 days.    USE - Low-carbon composite biological organic silicon-magnesium-potassium fertilizer.    ADVANTAGE - The fertilizer reduces usage of pesticide, increases product yield, improves product quality, improves soil cultivate fertilizer fertility, and has high quality and yield of agricultural products.
NOVELTY - Method for extracting natural taurine involves adding scallop as raw material, drying with high speed pulverizer, pulverizing the powder in distilled water at 55-80 degrees C, performing thermal water bath for 1-3 hours, collecting supernatant by filtration, adding collected supernatant to the activated carbon, collecting supernatant by filtration, adjusting the pH of collected supernatant, removing the supernatant, precipitating protein, concentrating supernatant under reduced pressure, and purifying.    USE - Method for extracting natural taurine (claimed).    ADVANTAGE - The method efficiently extracts natural taurine with high nutritive value without polluting the environment, by a simple method.    DETAILED DESCRIPTION - Method for extracting natural taurine involves adding scallop as raw material, drying with high speed pulverizer, pulverizing the powder in distilled water at 55-80 degrees C, performing thermal water bath for 1-3 hours, collecting supernatant by filtration, adding collected supernatant to the activated carbon, collecting supernatant by filtration, adjusting the pH of collected supernatant, removing the supernatant, precipitating protein in the acidic and basic proteins precipitate, collecting the supernatant by filtration, concentrating supernatant under reduced pressure, and purifying resulting concentrate by natural treatment.
NOVELTY - Synthesizing quinazolinone compound (I), involves reacting bronsted-acid and anthranilamide compound into vacuum reaction vessel, filling oxygen, then adding solvent and amine, sealing, heating at 10-40 degrees C for 1-40 hours, then cooling it to room temperature, after reaction to room temperature, extracting with water or saturated salt solution, drying and then decompressing and distilling using organic solvent, and then concentrating to remove the solvent, separating crude product by column chromatography to obtain the compound (I).    USE - For synthesizing quinazolinone compound (claimed) which is used as an anti-tumor agent.    ADVANTAGE - The method does not need metal as catalyst; uses raw materials which are cheap and easy to get; uses mild reaction condition; is green and environment-friendly; provides high selectivity and yield of product; and has good industrial application prospect.    DETAILED DESCRIPTION - Synthesizing quinazolinone compound of formula (I), involves reacting bronsted-acid and anthranilamide compound into vacuum reaction vessel, filling oxygen, then adding solvent and amine, sealing, heating at 10-40 degrees C for 1-40 hours, then cooling it to room temperature, after reaction to room temperature, extracting with water or saturated salt solution, drying and then decompressing and distilling using organic solvent, and then concentrating to remove the solvent, separating crude product by column chromatography to obtain the compound (I).    R1=H, methyl or phenyl;    R2=1-8C alkyl, phenyl, para-chlorophenyl, bromophenyl, p-methylphenyl, naphthyl, pyridinyl or benzothienyl.
NOVELTY - Preparing eletriptan involves reacting ethenesulfonyl-benzene and 5-bromo-1H-indole in presence of catalyst and acid-binding agent for 5-12 hours to obtain 5-((E)-2-benzenesulfonyl-vinyl)-1H-indole; condensation of 5-((E)-2-benzenesulfonyl-vinyl)-1H-indole and N-benzyloxycarbonyl-prolyl chloride to obtain (E)-benzyl 2-(5-(2-(phenylsulfonyl)vinyl)-1H-indole-3-carbonyl)pyrrolidine-1-carboxylate; and then reducing by using reducing agent, crystallizing and refining with ethanol to obtain eletriptan.    USE - For preparing eletriptan (claimed).    ADVANTAGE - The method is green and environment friendly, economically efficient, low cost and provides better quality of a triptan.
NOVELTY - An anhydrous dasatinib nigeria is synthesized by adding N-(2-chloro-6-methyl-phenyl)-2-((6-chloro-2-methyl-4-pyrimidinyl)amino)-5-thiazole carboxamide into dimethyl formamide and N-methylpyrrolidone mixed solvent, adding potassium iodide, adding potassium carbonate or sodium carbonate or triethylamine, heating, stirring, dropwise addition of N-hydroxyethyl-piperazine, letting to stand, thermal reaction, filtering, cooling, adding ethanol-water mixed solvent, cooling, crystallization, suction filtration, washing with ethanol-water mixed solvent, filtered to dryness, and purification.    USE - Synthesis of anhydrous dasatinib nigeria (claimed).    ADVANTAGE - Synthesis is simple, mild reaction condition, low production cost, environment-friendly, suitable for industrial production, and product obtained is of high purity.    DETAILED DESCRIPTION - An anhydrous dasatinib nigeria is synthesized by adding N-(2-chloro-6-methyl-phenyl)-2-((6-chloro-2-methyl-4-pyrimidinyl)amino)-5-thiazole carboxamide of formula I into dimethyl formamide (DMF) and N-methylpyrrolidone mixed solvent, adding potassium iodide as catalyst, adding potassium or sodium carbonate or triethylamine, heating at 60-65 degrees C, stirring for 0.5 hours, dropwise addition of N-hydroxyethyl-piperazine of formula (II) in DMF, letting to stand for 1 hour, thermal reaction to completion for 6-7 hours, detecting reaction progress by high performance liquid chromatography (HPLC), filtering while hot, cooling to 40-45 degrees C, adding ethanol-water mixed solvent at volume ration of 2:1, cooling to 5-10 degrees C, crystallization under stirring for 2 hours, suction filtration, washing obtained solid with ethanol-water mixed solvent, filtered to dryness to obtain crude aqueous dasatinib, and purification. Chemical reaction is shown in figure (I)..    DESCRIPTION OF DRAWING(S) - The drawing shows an X-ray diffraction pattern of dasatinib anhydrate powder. (Drawing includes non-English language text).
NOVELTY - A (3S,8aS)-3-(4-hydroxybenzyl)hexahydropyrrolo(1,2-a)pyrazine-1,4-dione (I) derived from Lysobacter enzymogenes, is new.    USE - The (3S,8aS)-3-(4-hydroxybenzyl)hexahydropyrrolo(1,2-a)pyrazine-1,4-dione is useful for preparing fungicide, and medicine for treating food poisoning by inhibiting aflatoxin produced by Aspergillus flavus or Candida albicans, and also useful for treating mucosal candidiasis, or internal organs and central nervous system candidiasis (all claimed).    ADVANTAGE - The method is simple in operation process by using biological method, short production period, cost-effective, and environmentally-friendly.    DETAILED DESCRIPTION - A (3S,8aS)-3-(4-hydroxybenzyl)hexahydropyrrolo(1,2-a)pyrazine-1,4-dione of formula (I) derived from Lysobacter enzymogenes, is new.
NOVELTY - Water is added to D-arabinose, pH is adjusted and reacted, to obtain heterogeneous solution. Activated carbon is added to obtained heterogeneous solution, incubated, bleached, filtered and purified using anion resin and cation resin to remove impurities, to obtain dried product containing 20-40 %mass D-ribose. Chromatography purification process is performed for obtained product, to obtain purified liquid comprising 75 %mass or more D-ribose. The obtained product is concentrated, ethanol is added, cooled, crystallized and centrifuged, to obtain D-ribose crystals.    USE - Manufacture of D-ribose crystals used for medicine and chemical industry.    ADVANTAGE - The method efficiently provides D-ribose crystals by economical and environmentally-friendly process.    DETAILED DESCRIPTION - Water is added to D-arabinose, to obtain aqueous solution having concentration of 10-30%. 0.5-1.2 %mass ammonium molybdate is added to adjust the pH to 2.5-4.8 and reacted at 80-130 degrees C for 1-3 hours, to obtain heterogeneous solution. 1-5 wt.% Activated carbon is added to obtained heterogeneous solution, incubated at 60-80 degrees C, bleached, filtered and purified using anion resin and cation resin to remove impurities, to obtain dried product containing 20-40 %mass D-ribose. Chromatography purification process is performed for obtained product, to obtain purified liquid comprising 75 %mass or more D-ribose. The obtained product is concentrated under vacuum, ethanol is added to obtained concentrate at 75 degrees C, stirred, cooled at 0.5-5 degrees C/hour, crystallized and centrifuged, to obtain D-ribose crystals.
NOVELTY - A bio-enzyme-containing diesel fuel additive composition comprises pour point depressants and bio-enzymes in the weight ratio of 1:0.01-10. The pour point depressant is a polymerization inhibitor containing vinyl acetate, ethylene, and olefin-based compound. The bio-enzymes contain alcohol oxidase, aldehyde oxidase, amine oxidase, sulfhydryl oxidase, methanethiol oxidase, menaquinone oxidase, peroxidase, demethylase, decarboxylase, aldolase, oxo-acid-lyase, sulfo-enzymes, magnesium chelatase, and/or alcohol, acid, or ester dehydratase.    USE - Bio-enzyme-containing diesel fuel additive composition (claimed).    ADVANTAGE - The bio-enzyme-containing diesel fuel additive composition has excellent pour point depressing effect and catalytic performance, and provides the diesel oil with excellent performance.    DETAILED DESCRIPTION - A bio-enzyme-containing diesel fuel additive composition comprises pour point depressants and bio-enzymes in the weight ratio of 1:0.01-10. The pour point depressant is a polymerization inhibitor containing vinyl acetate, ethylene, and olefin-based compound. The bio-enzymes contain alcohol oxidase, aldehyde oxidase, amine oxidase, sulfhydryl oxidase, methanethiol oxidase, menaquinone oxidase, peroxidase, demethylase, decarboxylase, aldolase, oxo-acid-lyase, sulfo-enzymes, de-sulfhydryl enzymes, desulfurization demethylase, ferrochelatase, cobalt-chelating enzymes, magnesium chelatase, and/or alcohol, acid, or ester dehydratase.
NOVELTY - Microbial composition for fermenting waste including animal excrement, dairy manure, pig manure, and chicken manure contains Cellulomonas fabia, Bacillus sterothermophilus, Lactobacillus, Methanobacterium Thiobacillus, B.licheniformis, B.polymyxa, Streptomyces, Thermonospora, Rhizobium, Aspergillus oryzae, Saccharomyces, Penicillium, Rhizopus, Lactobacillus casei, and T.thiooxidans S.thermophilus.    USE - The microbial composition is useful for fermenting waste including animal excrement, dairy manure, pig manure, and chicken manure and providing anti-cropping and/or anti-greet stubble effects of organic fertilizer (all claimed).    DETAILED DESCRIPTION - Microbial composition for fermenting waste including animal excrement, dairy manure, pig manure, and chicken manure comprises Cellulomonas fabia, Bacillus sterothermophilus, Lactobacillus, Methanobacterium Thiobacillus, B.licheniformis, B.polymyxa, Streptomyces, Thermonospora, Azotobacter, Nitrosomonas, Nitrobacter, Rhizobium, Aspergillus oryzae, Saccharomyces, Penicillium, Rhizopus, Lactobacillus casei, M.formicium M.ruminantium, T.thiooxidans S.thermophilus, Thermoactinomyces vulgaris, Thermonospora curvata, Azotobacter vinelandii R.japonicum R.leguminosarum Saccharomyces cerevisiae, R.oligosporus, Rhizoctonia cerealis, Thiobacillus ferrooxidans, B.polymyxa, Thermoactinomyces vulgaris Azotobacter vinelandii, Nitrosomonas europeae, and Rhizobium japonicum.
NOVELTY - This utility model claims a household garbage fertilizer device, comprising a machine frame, a power device, a disc, a crushing device and a vibration separating sieve, wherein the metal frame is provided with a strain and strain spray head, the power device comprises a motor, a rotating main shaft, a rotating shaft and a gear box, a crushing device comprises a knife rest, a fixed blade and an iron mesh, the utility model is a device with magnetic disk capable of sieving the steel from the domestic garbage and so on is provided with a separating sieve in the domestic garbage, a plastic and can be used as organic fertilizer organic matter separated from the utility model device can automatically the household garbage spraying biological strain, organic matter and fermentation organic fertilizer, the utility model device is simple and practical, and the cost is low.
NOVELTY - This utility model claims a groove type composting ozone gas collecting and processing device comprises fertilizer slot, the fertilizer tank is provided with skirt, the skirt is connected with a draught fan through wind pipe connected with cyclone dust collector, a cyclone dust collector, a draught fan connected to deodorization tower, the deodorization tower is biological filter pool. The upper part of the hood is provided with air suction pipe, the air suction pipe is connected with the wind pipe. One side of the composting groove is connected with an air blower. A skirt connected to the stack fertilizer groove passes through curtain. This utility model uses the ozone collecting system to prevent the diffusion of odour, the deodorization tower and a biological filter tank and a gas, the system is featured with simple structure, reasonable layout, suitable for the organic solid waste aerobic composting deodorization nitrogen preserving type generated by collecting and processing the stench.
NOVELTY - This utility model claims a kind of tilt sludge fermentation storehouse, comprising the sealing structure, the top of the bin can be opened and closed a cabin cover, a sludge device, a sludge output device, the fermentation chamber is divided into a plurality of at least one of the inclined drawing block, the bottom of the fermentation chamber is provided with a ventilating plate, the ventilating plate is provided with an air inlet hole, the air inlet hole is connected with air inlet device, the bottom of the fermentation chamber is further provided with a water discharging pipe.
NOVELTY - Livestock and poultry excrement is decomposed in situ by mixing lactic acid bacteria, Bacillus subtilis, Candida utilis, photosynthetic bacteria, Actinomycetes and acetic acid bacteria, adding wheat bran, fermenting, adding methionine and lysine, mixing, and adding corn flour; laying on livestock pen, laying sawnwood, peanut shells and rice husk, and spreading bacterial culture; and mixing, covering, spraying water, and fermenting.    USE - Method for decomposing livestock and poultry excrement in situ (claimed) used as bactericide and fertilizer.    ADVANTAGE - The method reduces antibiotic use, pollution, water consumption and production cost.
NOVELTY - Biological organic fertilizer comprises microorganism strain, culture medium and livestock excrement. Microorganism strain is silicate microbial inoculum, organic matter-decomposing inoculant, and biological repairing agent at ratio of 1:1:0.25. Excrement is cattle manure, organic matter of more than 45%, and water content of less than 25%.    USE - Biological organic fertilizer used for passivating heavy metal (claimed).    ADVANTAGE - The fertilizer reduces adsorption of crops to heavy metal, and reduces content of heavy metal in agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic fertilizer comprising pre-fermenting microorganism and culture medium, processing bacteria fermentation with livestock and poultry excrement, and carrying out secondary fermentation to prepare biological organic fertilizer.
NOVELTY - Vancomycin fermentation liquid is subjected to micro filtration using cation exchange resin and filtrate is eluted using high-concentration eluent and concentrated. Urea is added to high-concentration solution, stirred, urea is dissolved, and filtered to remove suspended particles. The pH of the obtained solution is adjusted to 7.9-9, stood, crystallized, and filtered to obtain vancomycin crystal.    USE - Manufacture of vancomycin crystal (claimed).    ADVANTAGE - The vancomycin crystal is easily manufactured with purity of more than 85% and yield of more than 85%, without affecting environment.
NOVELTY - Preparation of microbial organic fertilizer, involves (a) crushing organic raw materials into powder and adding activated carbon and bacterial mixture for composting, and (b) adding organic raw materials for the second time to the fermented product, and adding animal excrement and biogas residue, and composting using bacterial mixture, where the organic material is litter, food and feed waste, bark, kitchen waste, animal waste and crop straw.    USE - The method is useful for preparing microbial organic fertilizer (claimed).    ADVANTAGE - The microbial organic fertilizer changes soil physical, chemical and biological conditions, softens soil, promotes the formation of soil granule structure and improves soil permeability, and provides good environment for soil and plant growth.    DETAILED DESCRIPTION - Preparation of microbial organic fertilizer, involves (a) crushing organic raw materials into powder and adding activated carbon and bacterial mixture for composting, and (b) adding organic raw materials for the second time to the fermented product, and adding animal excrement and biogas residue, and composting using bacterial mixture, where the organic material is litter, food and feed waste, bark, kitchen waste, animal waste and crop straw, and the bacterial mixture comprises 20 pts. wt. yeast, 15 pts. wt. Bacillus subtilis, 18 pts. wt. Bacillus thuringiensis, 7 pts. wt. Nocardia, 7 pts. wt. Lactobacillus and 10 pts. wt. Pseudomonas or Rhodopseudomonas palustris.
NOVELTY - The utility model claims a garbage fermentation tank turning special device, comprising a bracket, a first rack, a second rack, a main shaft, a stirring rod, the stirring blade, driving part, are respectively provided with a first gear on the bracket of the left and right ends of the second gear on the bracket beside the first gear is provided with a first motor, a first gear and the transmission shaft of the first motor is engaged with the first gear and the second gear is provided with a main shaft, the main shaft are uniformly provided with a plurality of stirring rod, the stirring rod is welded with a stirring blade, the lower end of the bracket is provided with a support wheel, the lower side of the bracket is provided with a travelling crane on the travelling crane move is provided with a track, a track support wheel coupled to the moving vehicle is set at the lower end with a driving wheel is provided with a second motor is fixed on the beam at the lower end of the mobile travelling crane, connected with a coupling connected with the transmission shaft and the moving driving wheel of the second motor, the turning device total design, simple structure, high degree of mechanization, uniformly turning, suitable for popularization and application.
NOVELTY - The utility model claims a sludge ferment fertilizer manufacture system, the upper end of the pit is provided with a plurality of raw material storage tank, the bottom of the pit is provided with a first belt conveyor, of the pit is provided with a mixing device, said mixing device is arranged beside the heating fermentation device, front end of the fermentation device is connected with a heating furnace, mixing fermentation device and heating device is connected with the heat discharge end of the fermentation device is connected with a deodorizing device, heating fermentation device is provided with a side of the fermenting tank, heat discharging end of the fermentation device and fermentation tank, the fermentation tank is provided with a stacking, fermentation tank is provided with a sieving machine, a fermenting tank and sieving machine is connected with the lower end of the sieving machine is provided with a large material outlet and the back end of the finished product material outlet, a sieving machine is provided with a plastic air outlet, are provided with a returning belt machine on the lower end of the material outlet and the plastic air outlet, the lower end of the material outlet is provided with a fifth belt conveyor.
NOVELTY - Multifunctional seedling substrate comprises effective microorganisms (EM) bacteria fermenting corn straw, perlite, vermiculite and calcium, where the volume ratio of EM bacteria fermenting corn straw, perlite and vermiculite is 6:3:1, and the calcium is present in an amount of 10-20 g/m3.    USE - Used as multifunctional seedling substrate.    ADVANTAGE - The seedling substrate reduces the environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing multifunctional seedling substrate comprising crushing corn straw into 2-3 cm, adjusting carbon/nitrogen according to ratio of 30-20, spraying 1000 kg of cornstalk EM bacteria liquid, uniformly mixing the EM bacteria liquid, adding water until the water content is 60-70% and then covering with plastic film heat preservation and moisturizing to ferment at temperature of 30-40 degrees C.
NOVELTY - A microcapsuled microbial fertilizer is produced by crushing agricultural waste, controlling water content at 60-65%, adding fermentation agent, modulating, crushing, homogenizing, fermenting at pH of 5.6-6.2 for 30 days, turning every 2-3 days, and adding 5-10 wt.% mushroom residue, 6-10 wt.% straw ash and 600-1000 g/T arbuscular mycorrhizal inoculant. Agricultural waste is straw, bran, rice hull, cake, soybean meal, wood powder, peel or weed. Arbuscular mycorrhizal inoculant is Glomus mosseae, Glomus etunicatum and Glomus versiforme at weight ratio of 3:3:2.    USE - Method for producing microcapsuled microbial fertilizer (claimed).    ADVANTAGE - The fertilizer has prolonged effect time of more than 3 months, and increased utilization ratio by 15%.    DETAILED DESCRIPTION - A microcapsuled microbial fertilizer is produced by crushing agricultural waste, controlling water content at 60-65%, adding fermentation agent, modulating, crushing, homogenizing, fermenting at pH of 5.6-6.2 for 30 days, turning every 2-3 days, and adding 5-10 wt.% mushroom residue, 6-10 wt.% straw ash and 600-1000 g/T arbuscular mycorrhizal inoculant. Agricultural waste is straw, bran, rice hull, cake, soybean meal, wood powder, peel or weed. Fermentation agent is Cellulomonas flavigena, Lactobacillus casei, Azotobacter vinelandii, Rhizobium leguminosarum, Aspergillus niger, Aspergillus oryzae and Humicola insolens at a mass ratio of 1:0.8:1.2:1.4:0.6:0.8:1.2. Arbuscular mycorrhizal inoculant is Glomus mosseae, Glomus etunicatum and Glomus versiforme at weight ratio of 3:3:2.
NOVELTY - Organic fertilizer is produced by collecting manure, adding conditioner, adding water to water content of 55-60%, adding 2-3 wt.% fermentation agent, fermenting to maturity, further fermenting for 3 to 5 days, dehydrating, drying to water content of less than or equal to 30%, packaging, and storing.    USE - Method for producing organic fertilizer (claimed) for eliminating pathogens.    ADVANTAGE - The fertilizer has comprehensive nutrition, enhanced beneficial microorganism propagation, and reduced environmental impact.
NOVELTY - A biological organic fertilizer is produced by taking dead livestock and poultry, grinding, adding decomposing inoculum, heat treating at 140-180 degrees C for 13-15 hours under pressure of 7 kg/cm2, stir frying at 95-105 degrees C for 72-108 hours, separating bone, and crushing; pulverizing fiber, adding meat and bone meal, mixing, adjusting to carbon-to-nitrogen ratio of 25-40:1, adjusting moisture content to 45-55% and pH to 5.5-8.5, and adding 2-10% shell powder, 5-10% humic acid and 2-10% seaweed; adding decomposing inoculum, stirring, and fermenting; and drying, crushing, and screening.    USE - Biological organic fertilizer.    ADVANTAGE - The process is simple, low-cost, and environment-friendly. The fertilizer is safe and high quality.
NOVELTY - Solanaceous vegetable seedling substrate comprises main raw material and auxiliary material. Main raw material is cassava skin and starch residue. Auxiliary material is chicken manure and bran mixture or chicken manure and shell powder mixture. Cassava skin, starch residue, chicken manure and bran are at volume ratio of 4:3:2:1. Cassava skin, starch residue, chicken manure and shell powder are at volume ratio of 5:2:2:1.    USE - Solanaceous vegetable seedling substrate.    ADVANTAGE - The substrate has good permeability, good water and fertilizer holding capacity, and good nutrient supply. The process is environment-friendly and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solanaceous vegetable seedling substrate comprising taking raw materials, adding microbial fermentation inoculum, adjusting carbon-to-nitrogen ratio using urea, mixing, composting, airing, grinding, adding inorganic fertilizer, and stirring.
NOVELTY - High selenium and germanium fertilizer comprises 1-5 wt.% germanium-enriched Spirulina-selenium-enriched Ganoderma lucidum mycelium base fertilizer, 2-6 wt.% high-quality organic fertilizer, livestock manure, fermented vegetables, fruit leather and environmental enzyme composite base fertilizer, 3-7 wt.% soil fertility enhancer fertilizer, 4-8 wt.% livestock manure and distillery waste composite fertilizer and 74-90 wt.% broccoli fertility enhancer composite base fertilizer.    USE - High selenium and germanium fertilizer used for broccoli, rice, sugarcane, corn, tobacco, soybean, vegetables and fruit trees (claimed).
NOVELTY - An organic fertilizer comprises 30-70 wt.% dry traditional Chinese medicine dregs, 0.01-0.5 wt.% biological bacteria, 20-40 wt.% peat, 10-30 wt.% lignite, 1-5 wt.% mineral fertilizer, and 0.1-0.5 wt.% functional bacteria.    USE - An organic fertilizer used for crops.    ADVANTAGE - The organic fertilizer improves crop quality and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer, comprising:    (A) drying to adjust moisture content of 50-70% dry traditional Chinese medicine dregs to 50-60%;    (B) uniformly mixing dry traditional Chinese medicine dregs, biological bacteria, peat, lignite, mineral fertilizer, and functional bacteria;    (C) carrying out aerobic fermentation at 50-70 degrees C for 10-15 days; and    (D) drying, crushing, sieving, and packaging.
NOVELTY - A culture medium comprises 73-77 wt.% rice straw, 11-13 wt.% corn cob, 6-8 wt.% potato, 3-5 wt.% brewer's grains, 0.3-0.5 wt.% glucose, 0.5-0.9 wt.% quicklime, 1-1.5 wt.% slaked lime, 0.5-1 wt.% agar, 0.5-1 wt.% peptone, 0.1-0.2 wt.% calcium superphosphate, and 0.1-0.2 wt.% magnesium sulfate.    USE - A culture medium used for mushroom (claimed).    ADVANTAGE - The culture medium is easy to prepare, and increases annual production of mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the culture medium, comprising uniformly mixing rice straw, corn cob, potato, brewer's grains, glucose, quicklime, slaked lime, agar, peptone, calcium superphosphate, and magnesium sulfate; soaking in a fermentation pool for more than 30 days; and drying to obtain a moisture content of greater than or equal to 30%.
NOVELTY - Preparing almond cake comprises crushing the mung bean, squeezing and swelling, extruding, grinding into fine powder, separating protein isolates by enzymolysis at 50-60 degrees C for 3-5 hours and film separation coupling method for polypeptide activity of enzyme (protex 6L), where the enzymolysis pH value is 8-10, the substrate concentration is 7-9% and adding amount of enzyme is 5000-7000 U/g to obtain green active polypeptide and amino acid, carrying out spray drying to obtain active peptide powder, mixing active peptide powder, taurine, white sugar, oil, almond and peanut, baking and packing.    USE - The method is useful for preparing antifatigue almond cake (claimed).    ADVANTAGE - The method produces almond cake with strong stability, high reliability and increased yield and rate in eco-friendly manner.    DETAILED DESCRIPTION - Preparing almond cake comprises crushing a mung bean, then roughly crushing the mung bean powder, squeezing and swelling, extruding and grinding into a fine powder, separating protein isolates by enzymolysis at a temperature of 50-60 degrees C for 3-5 hours and film separation coupling method for polypeptide activity of the enzyme (protex 6L), where the enzymolysis pH value is 8-10, the substrate concentration is 7-9% and the adding amount of enzyme is 5000-7000 U/g to obtain green active polypeptide and amino acid, carrying out spray drying to obtain the active peptide powder, mixing 10-40 pts. wt. of active peptide powder, 1-3 pts. wt. of taurine, 8-10 pts. wt. of white sugar, 3-9 pts. wt. of oil, 2-4 pts. wt. of almond and 2-4 pts. wt. of peanut, baking and packing.
NOVELTY - Manufacture of nifuratel involves cyclizing 1-hydrazino-3-methylthio-2-propanol and dimethyl carbonate using sodium methoxide, forming 3-amino-5-methylthio-2-oxazolidinone, diethyl-5-nitrofurfural is hydrolyzed to form 5-nitrofurfural, condensing 3-amino-5-methylthio-2-oxazolidinone and 5-nitrofurfural by liquid condensation method, forming crude product, dissolving resulting crude product in glacial acetic acid, bleaching with activated carbon, recrystallizing, washing with purified water and vacuum-drying.    USE - Manufacture of nifuratel (claimed).    ADVANTAGE - The environmentally-friendly nifuratel is manufactured efficiently and economically with high reaction efficiency, high yield, high purity and excellent productivity, by simple method.
NOVELTY - A traditional Chinese medicine composition for treating hemorrhoids, comprising medicine raw materials: 2-10 pts. wt. talc, 2-10 pts. wt. borax, 3-11 pts. wt. rhizoma coptidis, 1-5 pts. wt. rhizoma arisaematis, 3-11 pts. wt. Ootheca mantidis, 1-9 pts. wt. mung bean and 10-50 pts. wt. erythromycin ointment, is prepared by mechanical crushing or grinding talc, borax, coptis root, rhizoma arisaematis, Ootheca mantidis and mung bean according to prescription proportion into fine-like face ash powder, mixing it with erythromycin ointment to obtain a corresponding amount.    USE - As traditional Chinese medicine composition for treating hemorrhoids (claimed).    ADVANTAGE - The raw material medicine obtained has no high cost. The manufacturing method is simple, energy-saving and environment-friendly. The traditional Chinese medicine can treat inner hemorrhoids, and where the cure rate is up to or more than 90% and the time of the treatment is only a number of months; does not need surgery treatment, as compared to western medicine; as compared to western medicine is more low cost treatment for treating atrial fibrillation through labyrinth surgery and without surgery.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the traditional Chinese medicine involving: 1) mechanical crushing the raw materials, talc, borax, borneol, rhizoma coptidis, rhizoma arisaematis, Ootheca mantidis, mung bean, or grinding them into fine-like face ash powder; 2) mixing, fully stirring and mixing uniformly according to the proportion of part by weight; 3) mixing powder and ointment according to total weight of the mixture powder and erythrocin ointment by weight ratio of 1:1, mixing fully and uniformly stirring, sealing the container, for 7-10 days, and then setting by measuring into small package for treating hemorrhoids.
NOVELTY - A carbon ball catalyst comprises uniformly loaded auxiliary agents on its surface.    USE - Carbon ball catalyst used for preparing low carbon olefins via Fischer-Tropsch synthesis (claimed).    ADVANTAGE - The catalyst is easy to prepare, easy to control, has high mechanical strength, exhibits high catalytic activity, and has high selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of carbon ball catalyst comprising mixing ion exchange resin microsphere, precursor and catalyst, stirring, removing residual catalyst and precursor, drying under inert atmosphere, and roasting.
NOVELTY - Preparing biological fertilizer using domestic sludge involves calculating volume of sludge to 0-30 vol.% with water content is not more than 85%; pre-treating auxiliary material using high mass of mushroom residue, wooden meal, rice bran, slag and lignin or cellulose; using self-researched for sludge fermentation organic matter-decomposing inoculant; making domestic sludge and adjusting moisture to 50-65%; fermenting, aging, crushing, sieving and packaging.    USE - For preparing biological fertilizer using domestic sludge (claimed).    ADVANTAGE - The method is simple and practical, avoid greater extent the organic matter, salt, and rotten free yeast so as to burn, produce the biological fertilizer relative to e.g. to has good profit creativity and use effect than same type organic fertilizer. The method prepares fertilizer using low organic matter, easy fermentation; improves the initial fermentation temperature, quickly raising the temperature and shortens fermentation period; effectively relieve the problem of salt sludge and improve soil and promote the growth of crops, has good fertilizer effect.    DETAILED DESCRIPTION - Preparing biological fertilizer using domestic sludge involves: calculating volume of sludge to 0-30 vol.% with water content is not more than 85%; pre-treating auxiliary material using high mass of mushroom residue, wooden meal, rice bran, slag and lignin or cellulose; using self-researched for sludge fermentation organic matter-decomposing inoculant; making domestic sludge, by processing auxiliary material, and organic matter-decomposing inoculant, and adjusting the moisture to 50-65%; fermenting for the first time so that the central temperature reach 65 degrees C and is kept for 3 more days; carrying out continuous fermentation in the production process and returning to fermentation; fermenting for the first time and enter aging period by adding functional strain; aging, crushing, sieving and packaging.
NOVELTY - Method for producing vermicompost by processing straw, involves crushing straw, mixing crushed straw and rotten chicken manure in a weight ratio of 2.5:1 to obtain mixture, pre-fermenting the mixture at 30 degrees C for 15 days, inoculating earthworm to pre-fermented product, maintaining temperature at 25 degrees C and water content of 55 plus minus 5%, and composting the material for 60 days to obtain organic fertilizer.    USE - The method is useful for producing vermicompost by processing straw (claimed), where the vermicompost is used for providing fertilizing effect.    ADVANTAGE - The method improves straw processing rate.
NOVELTY - Processing died animal comprises collecting died animals and animal waste, preparing gold needle mushroom residue, sawdust and rice hull, mixing the prepared materials into a fermentation tank and adding with corn flour and animal tissue, mixing the mixed materials with an inoculant to obtain fermentation material, and embedding the died animal body with the obtained fermentation material to ferment for 35-50 days.    USE - The method is useful for processing died animal including dead poultry animal body or livestock animal including bovine, sheep, rabbit chicken and duck body (all claimed).    DETAILED DESCRIPTION - Processing died animal comprises collecting died animals and animal waste, preparing gold needle mushroom residue, sawdust and rice hull, mixing the prepared materials into a fermentation tank and adding with corn flour and animal tissue, mixing the mixed materials with an inoculant to obtain fermentation material, and embedding the died animal body with the obtained fermentation material to ferment for 35-50 days, where the animal tissue decomposition agent is 1x 108-9 colony-forming unit (cfu)/m3 of Bacillus cereus, 1x 107-8 cfu/m3 of thermophilic fungi, 1x 107-7 cfu/m3 of thermophilic Actinomycetes.
NOVELTY - A primary culture material comprises 30-40 wt.% cotton seed hull, 30-40 wt.% sawdust, 18-22 wt.% bran, 0.5-1.1 wt.% calcium carbonate, 0.5-1.1 wt.% sugar, and culture medium having natural pH value.    USE - Primary culture material used for Panus giganteus (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivation of mushroom comprising cultivating mushroom in bag for 10 days at stable temperature of 20 degrees C, using burnt soil, paddy soil, or vegetable garden soil, where top soil thickness is 3-4 cm and 1.5-2 cm soil diameter, adding water to adjust moisture of soil, excavating 2-3 cm, and planting mushroom.
NOVELTY - Manufacturing flower and plant nutrient base, involves: 1) taking 1 m3 straw, crushing 0.1-1 cm pulverized particles; 2) adding 2 L Bacillus subtilis, same time adding 90-95 L tap water, making micro-organism liquid; 3) putting straw particle into fermentation tank, adding 3-5 kg nitrogenous fertilizer, 2-3 kg potash fertilizer, and 2-3 kg phosphate fertilizer, stirring/spraying micro-organism liquid to particle; 4) after every 12 hours, turning straw stack, fermenting; and 5) taking product, drying, uniformly adding 50-60 kg powder to obtain flower nutrient matrix.    USE - For manufacturing flower and plant nutrient base (claimed).    ADVANTAGE - The method is featured with simple operation, good for popularization; uses straw crushing, then putting in a fermentation tank to ferment by microorganism, which can quickly make straw into organic small molecule, degrade cellulose bacillus where the culture condition is simple, fast growth, which can ensure the rapid degradation of straw, shortens the production period, nutrient matrix; and avoid straw burning process caused by the surface environment and atmospheric environment.    DETAILED DESCRIPTION - Manufacturing flower and plant nutrient base, involves: 1) taking 1 m3 straw, crushing 0.1-1 cm length of pulverized particles by a crusher; 2) adding 2 liter Bacillus subtilis, same time adding 90-95 liter tap water, making micro-organism liquid; 3) putting straw particle into fermentation tank, adding 3-5 kg nitrogenous fertilizer, 2-3 kg potash fertilizer, and 2-3 kg phosphate fertilizer, stirring uniformly, spraying micro-organism liquid towards the straw particles; 4) after every 12 hours, turning the straw stack, removing heat, and fermenting for 15-20 days; and 5) taking out fermentation product, drying, uniformly adding 50-60 kg powder in the drying process to obtain flower nutrient matrix.
NOVELTY - Selenium-enriched bio-organic fertilizer comprises 75-80 mass% of earthworm manure, 10-15 mass% of sodium, 5-10 mass% of humic acid and 2-3 mass% of biological fermentation bacteria.    USE - The selenium-enriched bio-organic fertilizer is useful for promoting growth of crops.    ADVANTAGE - The selenium-enriched bio-organic fertilizer is safe and environmental friendly, and has good quality, high yield, no toxicity and no residue.
NOVELTY - Producing organic fertilizer comprises (a) inoculating Bacillus subtilis in a liquid medium containing pectin as a carbon source to obtain liquid inoculant medium, (b) mixing liquid inoculants, citrus peel, water regulator and pH adjusting agent into a fermentation tank to obtain a microbial inoculum mixture A, (c) mixing purple mudstone with the pH adjusting agent to obtain a mixture A, and (d) adding mixture A, citrus peel and water and then heating in a greenhouse for composting fermentation until the moisture is reduced to 20% to obtain organic fertilizers.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The method produces the organic fertilizer with rapid microorganism decomposition rate and good odor and ammonia absorbing rate.    DETAILED DESCRIPTION - Producing organic fertilizer comprises (a) inoculating Bacillus subtilis in a liquid medium containing pectin as a carbon source to obtain liquid inoculant medium, (b) mixing liquid inoculants, citrus peel, water regulator and pH adjusting agent in the ratio of 1:5-9:1-3:0.5-1.5 into a fermentation tank to obtain a microbial inoculum mixture A, (c) mixing purple mudstone with the pH adjusting agent in the ratio of 1-5:1 to obtain a mixture A, and (d) adding mixture A, citrus peel and water in the ratio of 1:1-3:50-150:0.5-1.5 and then heating in a greenhouse for composting fermentation until the moisture is reduced to 20% to obtain organic fertilizers.
NOVELTY - A red mushroom cultivation material, comprises: 30-40 wt.% tea seed meal, 20-30 wt.% tea root meal, 20 wt.% cotton seed hull, 12 wt.% rice bran, 5 wt.% tea seed, 2 wt.% Phellodendron, and 100 wt.% gypsum powder and lime powder both in dry matter proportion.    USE - As red mushroom cultivation material (claimed).    ADVANTAGE - The cultivation material thickness are reasonable and improves air permeability, promote the formation of red mushroom fruit body original base to make a mushroom, widens the planting raw material, and greatly reduces the production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cultivation material, involving: mixing fungi with the raw material exposure for 1-2 days using ultraviolet, under uniform stirring, carrying out pre-wet with 1% lime water solution, stacking ferment, drying 300-500kg culturing material, cover the upper part of the tarpaulin to make it natural ferment, turning when the material temperature reaches 60 degrees C, keeping for 24 hours, adding cotton seed hull, rice bran, tea seed, Phellodendron, gypsum powder and auxiliary material, and water, turning 4-5 times for 6-7 days, stop fermenting, sterilizing and cooling the material to normal pressure sterilization, when temperature reaches 100 degrees C, discharge cooling gas, keeping for 8-10 hours, then naturally cool to lower than 25 degrees C.
NOVELTY - Manufacturing nutrient soil, is claimed, where the nutrient soil comprises 65 wt.% of honeycomb slag, 15 wt.% of chicken manure, 12 wt.% of weed leaf, 5 wt.% of Commelina, 1 wt.% of fertilizer, 0.4 wt.% of insecticide, 0.3 wt.% of fungicide and herbicide and 1 wt.% of ferrous sulfate and then cutting.    USE - The method is useful for manufacturing nutrient soil (claimed), which is useful for cultivation planting flower and vegetable seedlings.    ADVANTAGE - The method manufactures nutrient soil with rich in nutrition in a simple manner.
NOVELTY - Microbial fertilizer containing amino acid comprises 600-750 pts. wt. composite microbial strain, 100-150 pts. wt. urea, 50-150 pts. wt. potassium sulfate, 50-150 pts. wt. diammonium phosphate and 100-200 pts. wt. amino acid solution, where the fertilizer comprises 60-75 wt.% microbial strain.    USE - The microbial fertilizer containing amino acid is useful for enhancing plant disease resistance and stress resistance in small cabbage and tobacco (claimed).    ADVANTAGE - The fertilizer improves soil fertility and promotes nutrient absorption of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the microbial fertilizer, which involves obtaining the raw materials, crushing the materials, then mixing with solvent to obtain amino acid solution, adding Bacillus subtilis, B.licheniformis and B.megaterium, intermittently stirring to obtain activated mixed solution, mixing the activated liquid and packaging to obtain compound microbial fertilizer containing amino acid.
NOVELTY - Method for preparing biological fertilizer rich in trace elements, involves using straw powder, animal manure, ammonium nitrate and water as raw materials, mixing the raw materials with complex microorganisms and trace elements, fermenting the mixture (primary fermentation), turning the mixture, performing secondary fermentation, adding trace elements to the fermented material, and bagging the product.    USE - The method is useful for preparing biological fertilizer rich in trace elements which is useful for Chrysanthemum. The trace elements are selenium, chromium, zinc, manganese or boron (all claimed).    ADVANTAGE - The method is simple and cost-effective. The biological fertilizer prepared by the method improves soil structure, soil environment, photosynthetic function, and quality of Chrysanthemum.
NOVELTY - Porous, organic fertilizer is prepared by fermenting plant straw, animal excrement, edible fungi residues and lees using microorganisms to obtain organic material, and then crushing and extruding the organic material to obtain the product.    USE - The porous, organic fertilizer is useful for agricultural planting field.    ADVANTAGE - The organic fertilizer has good water absorbing and retaining property, improves soil ecological environment, and is convenient to transport and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing porous organic fertilizer, which involves collecting edible fungi residues, crushing, mixing the crushed edible fungi residues with water, adding microorganisms, fermenting the mixture for 30-45 days by turning once every 15 days, obtaining the decomposed raw material and fermented material combined edible fungi residues, drying until the water content is 20-40% and obtaining the organic fertilizer.
NOVELTY - Oxime synthesis of nitrile comprises reacting selenium compound catalyst and aldehyde oxime in solvent at 30-100 degrees C, heating, dehydrating, distilling and purifying.    USE - Method for oxime synthesis of nitrile used for medicine synthesis and production of fine chemical intermediate (claimed).    ADVANTAGE - The method has easy to obtain raw material, high yield, economical and environment-friendly operations.
NOVELTY - 1-(4-Halo-phenyl)-1H-pyrazole compound (I) is new.    USE - As antiseptic agent.    ADVANTAGE - The compound is prepared by few reaction steps and low cost method, utilizes cheap and easily obtained raw material, has simple technique operation, provides high purity and yield of the product, has mild reaction condition, and is green and pollution-free.    DETAILED DESCRIPTION - 1-(4-Halo-phenyl)-1H-pyrazole compound (I) is new.    R1 and R2=alkyl;    X=halogen.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Separating and purifying ginkgolides C, involves: (1) extracting ginkgo biloba leaf extract using organic solvent; (2) back extracting GEL CHP MC1-series macroporous absorption resin, eluting with 0-20 wt.% ethanol to remove impurity, collecting ginkgolides C eluent; (3) evaporating to obtain ginkgolide C crude product, recycling solvent, adding product to 10-90% ethanol, at 40-70 degrees C and completely dissolving the product, filtering/refrigerating for 12-48 hours at 2-10 degrees C, separating crystal, crystallizing for 1-3 times, washing, vacuum heating at 60-120 degrees C and drying.    USE - For separating and purifying ginkgolides C (claimed) used for industrial production.    ADVANTAGE - The method of separating and purifying ginkgolides C solvent is easy; uses conventional equipment, so the operation is simple, has less energy consumption, low cost, is made of non-toxic adsorbent, so production is safe, and is pollution-free. The method obtain ginkgolides C having purity of more than 98%.    DETAILED DESCRIPTION - Separating and purifying ginkgolides C, involves: (1) extracting ginkgo biloba leaf extract by organic solvent extraction; (2) back extracting GEL CHP MC1-series macroporous absorption resin, firstly eluting them with 0-20 wt.% ethanol to remove impurity, then using 20-40% ethanol to elute resin, collecting ginkgolides C eluent; (3) decompressing/evaporating to obtain ginkgolide C crude product, recycling the solvent, adding 1/2-2 times of the crude product of 10-90% ethanol, at 40-70 degrees C and completely dissolving the crude product, filtering, refrigerating for 12-48 hours at 2-10 degrees C, separating out the crystal, repeating crystallizing for 1-3 times, washing 1-5 times with purified water, at 60-120 degrees C, vacuum heating and drying to obtain the ginkgolides C.
NOVELTY - A sludge carbon material is prepared by introducing high water content sludge to tank through sludge pump, discharging water vapor from reactor for direct or indirect heat exchange, preheating sludge in reactor, introducing saturated steam at 160-300 degrees C while stirring under pressure, carrying out viscous organic sludge hydrolysis, destroying gel structure and cell wall of sludge to separate bound water and solid particles and to obtain liquid slurry, pumping high pressure liquid slurry to buffer tank under pressure and temperature, separating bound water from solid particles, and dehydrating.    USE - Preparation of sludge carbon material for activated carbon used in sewage treatment plant adsorption and biochar production used as fertilizer and soil modifying agent (all claimed).    ADVANTAGE - The process is environment-friendly.    DETAILED DESCRIPTION - A sludge carbon material is prepared by introducing high water content sludge to tank through sludge pump, discharging water vapor from reactor for direct or indirect heat exchange, preheating sludge in reactor, introducing saturated steam at 160-300 degrees C while stirring under pressure, carrying out viscous organic sludge hydrolysis, destroying gel structure and cell wall of sludge to separate bound water and solid particles and to obtain liquid slurry, pumping high pressure liquid slurry to buffer tank under pressure and temperature, separating bound water from solid particles, dehydrating in frame filter press or centrifugal dehydrating machine to obtain reduced moisture content of 40%, feeding to granulating extruder, and carbonizing in pyrolytic carbonization furnace to obtain biochar.
NOVELTY - Producing biodiesel by ultrasonic-assisted direct transesterification of microalgae, comprises: (a) mixing dried algae powder with anhydrous methanol solution and potassium hydroxide catalyst, and (b) removing out the reaction solution obtained in the step (a), allowing to stand and cooling, filtering the algae powder, extracting with petroleum ether, adding saturated sodium chloride solution, allowing to stand and layering, collecting the upper petroleum ether phase, repeatedly extracting, combining the organic phases, vacuum extracting and distilling to obtain the biodiesel crude product.    USE - The method is useful for producing biodiesel by ultrasonic-assisted direct transesterification of microalgae (claimed).    ADVANTAGE - The method is simple, clean and environment-friendly; shortens the reaction time; and reduces the production cost.    DETAILED DESCRIPTION - Producing biodiesel by ultrasonic-assisted direct transesterification of microalgae, comprises: (a) mixing dried algae powder with anhydrous methanol solution in a solid to liquid ratio of 1:2-1:6 and potassium hydroxide catalyst accounting for 3-11 wt.% of the total weight of the algae powder, where the reaction temperature is 60-100 degrees C, the ultrasonic power is 400 W and the reaction time is 10-50 minutes, and (b) removing out the reaction solution obtained in the step (a), allowing to stand and cooling for 1-1.5 hours at room temperature, filtering the algae powder, extracting with petroleum ether, adding saturated sodium chloride solution, allowing to stand and layering, collecting the upper petroleum ether phase, repeatedly extracting for 3-4 times, combining the organic phases, vacuum extracting and distilling to obtain the biodiesel crude product.
NOVELTY - A Pantoea dispersa strain pt1 (CGMCC NO: 7595), is new.    USE - The P.dispersa strain is useful in microbial fertilizer for improving utilization rate of the fertilizer and soil structure, and increasing yield and quality of crops (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial fertilizer comprising the above-mentioned strain; and    (2) method for preparing the microbial fertilizer, involves preparing microbial inoculum by inoculating strain in nutrient-broth culture medium comprising 0.5% peptone, 0.3% beef paste, 0.5% sodium chloride and distilled water (remainder) and having pH 7, inoculating the seed culture in fermentation tank containing medium, and fermenting the mixture, where the fermentation medium comprises 15 g corn powder, 4 g glucose, 21 g bean cake powder, 4 g fish meal, 9 g calcium carbonate, 1.5 g ammonium sulfate, 0.5 g dipotassium phosphate, 0.1 g magnesium sulfate heptahydrate, 0.1 g sodium chloride and 1000 ml water and having pH of 7.5.
NOVELTY - A Pseudomonas fluorescens strain pt4 (CGMCC NO: 7597), is new.    USE - The P.fluorescens strain pt4 is useful in microbial inoculum for improving utilization rate of fertilizer, soil structure, and yield and quality of crops, and as microbial fungicide (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial inoculum; and    (2) method for preparing the above-mentioned microbial inoculum.
NOVELTY - A sludge treatment device, especially to a processing device and a post-processing device in the device, the sludge to form soil cultivating device. It is a processing device on the upper part of the shell, the upper part of pre-processing device is a feeding port, the lower part of the device inner part is crushing device, crushing drying device is added. A processing device depending on the guide tube connected with the processing device, the processing device is a stirring device, mixing fermentation device and material outlet. When using, the sludge into a processing device through a port, then rolling and drying by conduit entering into processing device, a sludge to form cultivation soil by adding material and subsequent fermentation process in the post-processing apparatus, so it is good for scientific sludge.
NOVELTY - This utility model claims a kitchen garbage processor is a cover and device, is provided with a feeding port at the upper part for processing kitchen waste tank above the connecting piece, the connecting piece, the feeding port is provided with a sealing cover which can be opened, connecting piece side wall is provided with a strip-shaped exhaust hole, the exhaust hole is located at a feeding opening, a connecting piece is set with a linkage and the sealing cover of the deodorizing element, component and a cross-flow fan, deodorizing module, fan is set on the exhaust hole for the connecting piece to form the negative pressure for the gas, a suction connecting piece, and a part is provided with the air outlet of the cross-flow fan. This utility model is a cover device effectively solves the problem that the kitchen garbage processor of the prior art emit peculiar smell when lid, and the deodorizing element and the sealing cover, the sealing cover is opened only when the cross-flow fan, the cover and power consumption of the device, the kitchen garbage processor of protecting environment and saving energy;
NOVELTY - This utility model claims a kind of organic matter from fermentation turning machine, comprising a cylinder body, a top cover, a bottom plate and a cylinder shaft tube, the top cover is provided with a feeding port, the feeding port is provided with a controlling amount is, the top cover is provided with a flange and the end part of the cylinder body, the top cover and the end part of the cylinder body by a bolt, the lower end of the cylinder end and cylinder bottom plate is fixed on the shaft tube is fixedly connected with a blade and a stirring rod, wherein the shaft tube is vertically set in the cylinder body, and the cylinder line perpendicular bisector, the upper end and the lower end of the shaft pipe are respectively connected with the top cover, a cylinder bottom. The organic matter from fermentation turning machine has reasonable design, simple structure, small occupied area, capable of realizing local production, it has low cost, large processing amount, high production efficiency, energy-saving, high degree of automation, easy to operate, safe and reliable and so on, at the same time, it reduces the pollution to the environment, strong practicability, with industrial production condition.
NOVELTY - This utility model claims a kind of small size farm organic fertilizer fermentation device, comprising a spot of a feeding hopper, a screw conveyor and an inclined conveyor, a fermentation chamber and a control box, the lower part of the storage bin is provided with a side wall provided with a discharging opening, the discharging opening is provided with a discharging amount of the manual valve, the feeding port of the screw conveyor is located below the discharge hole of the storage bin, the material for, and the screw conveyor is provided with a strain adding a microelement of automatic feeding device, the material outlet of the screw conveyor to an inclined conveyor, a discharging port of the inclined conveyor is provided with a rotatable bag bracket, wherein the organic waste treating machine according to the design is reasonable, the structure is simple, the implementation of local fermentation organic fertilizer and high production efficiency, and high degree of automation, which effectively reduces the production cost, at the same time reduce the pollution to the environment, it is more energy-saving and environment-friendly, with industrial production condition.
NOVELTY - The utility model claims a hydrolyzing-aerobic compost process system, comprising an anaerobic hydrolysis acidification reactor, a pH adjuster, an aerobic compost reactor, a feeding port of the pH adjuster anaerobic hydrolyzing acidifying reactor is connected to a port of the aerobic composting reactor the pH adjuster. This utility model is not completely anaerobic processing (only hydrolysis acidification stage) and the aerobic composting process are combined, it can reduce the energy consumption and simple aerobic treatment, and a simple anaerobic treatment, first anaerobic and aerobic treatment can obviously shorten treatment period, at the same time it can reduce the anaerobic process generating the odour.
NOVELTY - A kind of livestock and poultry farm organic waste processor, comprising a machine frame, a horizontal U-shaped barrel, a motor transmission mechanism, a main shaft, a turning mechanism, a loading mechanism, a feeding mechanism, a heating mechanism, wherein the main shaft is fixed 12 radial blade, the blade radial direction is an inclined plate-shaped, the cross section is space inclined angle with the main shaft, a radial blade connected end extending a 90 degree is a bent plate ;12 radial blades are spirally distributed, two radial blade space adjacent phase angle is 90 degrees, and the adjacent two radial blades and the main shaft axis of the space angle is mutually reverse negative angle, inner wall of the tube body at intervals in a 12 set of openings toward door-shaped damping of the main shaft, each group of a plurality of damping plate corresponding to the semicircular space in a radial blades are uniformly distributed, a horizontal U-shaped barrel is inner and outer double layer wall and the oil heater pipe is connected, wherein the radial blade is damping with a mashing the raw material yeast;
NOVELTY - The utility model relates to the technical field of producing amantadine hydrochloride, especially relates to one kind of hydrochloric acid adamantane amine in filter device, comprising a distillation kettle aminating and condenser, the amination distillation kettle is connected with the condenser, the condenser is connected with the material cylinder, wherein the material cylinder is connected with a plate-and-frame filter press through the knockout pump, the plate-and-frame filter press is connected with the condenser. This utility model is a new-type plate-and-frame filter press and filtering the mother liquid again into the condenser, it can realize continuous production, change in the prior art intermittent production mode, improves the production efficiency, a tube type condenser, wherein the condensing effect is better, the material will not phenomenon of hanging wall.
NOVELTY - Organic fertilizer comprises 10-20 mass% of tobacco scrap, 0.1 mass% of microbial inoculum and balance amount of livestock manure, where the tobacco scrap is processed as residue.    USE - Used as organic fertilizer.    ADVANTAGE - The organic fertilizer is prepared in a simple manner and eco-friendly, and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the organic fertilizer comprising crushing the tobacco scraps into particles of 5 mm or less using a crusher, mixing the above materials and placing into the fermentation tank provided with a sun shading shed, where the total moisture content of the livestock manure is 35-40%, uniformly mixing and stirring using fertilizer flap machine, carrying out fermentation at 70-80 degrees C for 10-20 days, mixing and stirring when the fermenting tank temperature is more than 80 degrees C and discharging the fertilizer having a moisture content of 15-25%.
NOVELTY - Preparing biological activating agent particle, comprises drying peat and grass by a roller drier, crushing the dried peat and grass by crusher, vibration sieving the crushed particles, again sieving to obtain macromolecule, passing crushed particle through 80 meshes to obtain small molecule, adding humic acid as reactant, pelletizing by pelletizer to obtain granule, spray-drying biological activating agent to adsorption humic acid, where the content of the humic acid in the bio-activator particle is more than 45%, and the biological agent is present in an amount of more than 25%.    USE - The biological activating agent particle is useful in fertilizer, which is useful for improving yield of plants such as corn, soybean, sugar beet and fruit tree (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of biological activating agent in fertilizer, where the bioactivator has bacillus particle having a viable count of more than 0.2 hundred million/g, mixed bacterium rate of less than 100/g and humic acid content of not less than 40%.
NOVELTY - This utility model claims a turning roller includes a roller body, and the upper part of the cylinder body is provided with multiple vertical is provided with a turning plate, turning plate is provided with a . The turning plate is provided with top end provided with M a crevasse and a rupture a sheet finishing crushing agglomeration organic fertilizer. The turning plate is spirally distributed on the roller cylinder body and improves the turning efficiency. Because of adopting said structure, by using the turning plate and a sheet, and make the procedure of crushing material in the work and improves the working efficiency.
NOVELTY - Method for preparing pesticide, involves using herbs and auxiliary agents, where the herbs are 28-38 kg star anise, 10-18 kg pepper, 14-20 kg Celastrus angulatus, 26-36 kg Selenastrum or 20-30 kg Chinaberry seed, auxiliary agents are 8-11 kg emulsifier, 9-15 kg turpentine oil, 4-6 kg penetrating agent, 0.6-1.5 kg preservative or 22-28 kg ethanol, and ratio of herbs and auxiliary agents are 1:1.    USE - The method is useful for preparing pesticide (claimed).    ADVANTAGE - The pesticide prepared by the method is environmentally-friendly, and does not produce secondary toxicity and residues.
NOVELTY - A copper (Cu)/copper oxide (CuxO)/titanium dioxide (TiO2) heterojunction visible light catalyst has spherical shape and particle diameter of 2-3 mu m.    USE - Copper/copper oxide/titanium dioxide heterojunction visible light catalyst used for degrading organic pollutant and killing Acinetobacter baumannii (all claimed).    ADVANTAGE - Cu/CuxO/TiO2 heterojunction visible light catalyst has uniform size, low carrier recombination rate, high photo-catalytic activity, and good stability, and preparation method is simple and environment-friendly, eliminates use of reducing agent, and reduces production cost.    DETAILED DESCRIPTION - A copper (Cu)/copper oxide (CuxO)/titanium dioxide (TiO2) heterojunction visible light catalyst has spherical shape and particle diameter of 2-3 mu m.    x=1 or 2.    An INDEPENDENT CLAIM is included for preparation of Cu/CuxO/TiO2 heterojunction visible light catalyst which involves mixing precursor of soluble copper salt and ethanol, stirring until soluble copper salt is dissolved, adding tetrabutyl titanate, continuing and stirring for 0.2-0.6 hours, injecting ethanol using supercritical alcohol technique for 50-90 minutes at 200-250 degrees C, cooling, washing, centrifugally separating, and drying.    DESCRIPTION OF DRAWING(S) - The drawing shows a scanning electron microscope image, enlarged scanning electron microscope image, and transmission electron microscope image of catalyst.
NOVELTY - This utility model claims a garbage processing system, especially claims a method for area of shutter glass window screen. Dry continuous anaerobic fermentation solution household garbage treating system, wherein the structure is as follows: hand picking garbage platform of garbage outlet end is connected with a garbage opening crushing separating tank, separating and crushing tank oxygen outlet and the fermentation pool, the separating tank is provided with a crushing machine, a crusher is provided with separating the upper part of the crushing tank is connected with the anaerobic fermentation solution tank for aerobic glycolysis, glycolysis. upper end is hermetically connected with a gas collecting tank, an anaerobic fermentation pool and the lower part is provided with a solid fertilizer outlet, with oxygen fermentation pool and the anaerobic fermentation pool, the lower end is provided with a scraper. multi-enzyme fermentation solution pool and collecting the solid fertilizer of the upper part of the rear end is provided with a liquid fertilizer outlet. This utility model passes through anaerobic treatment and the garbage into methane, carbon dioxide and fertilizer, does not pollute the environment, without a material outlet, the equipment investment is low, easy to manage.
NOVELTY - A biological organic fertilizer for tobacco is prepared by crushing the tobacco material into powder, then adding water, and biological fermentation agent, where the weight ratio of the biological fermentation agent and the tobacco material is 1:500-600, then fermenting 58-63 degrees C for 8-10 days, every 2-3 days turning one time, and where the water content of the tobacco material is 65-70%.    USE - As biological organic fertilizer for tobacco (claimed).    ADVANTAGE - The biological organic fertilizer has low cost; promotes root growth; and also improves the crop yield and crop quality.
NOVELTY - Removing antibiotic from pig manure comprises mixing 6-7 wt.% of dry sawdust, 5-6 wt.% of rotten manure, 0-9 wt.% of bamboo charcoal and 81-87 wt.% of fresh pig manure, where the ratio of carbon and nitrogen in the material is 21-25:1, adding water whose content is 60-65%, carrying out fermentation for every 5 days and a manual turning for 7 days, composting for 45 days at a stack temperature, drying by freezing, sieving and measuring antibiotic content.    USE - The process is useful for removing antibiotic from pig manure (claimed).    ADVANTAGE - The process has a high antibiotic removal rate of more than 90% and improves the quality of the fertilizer.
NOVELTY - A biological organic fertilizer specifically for leek, comprises: 400-500 pts. wt. dry rotten biogas residue, 80-120 pts. wt. grass carbon, 80-120 pts. wt. weathered coal, 40-60 pts. wt. molasses, 50-70 pts. wt. urea, 20-30 pts. wt. diammonium phosphate, 80-120 pts. wt. potassium sulfate, 51-137 pts. wt. kaolin, 800-1200 pts. wt. biogas, not less than 100 million/g Bacillus megaterium, not less than 500 million/g Bacillus mucilaginosus, and not less than 1000 million/g Paenibacillus polymyxa.    USE - As a biological organic fertilizer which is specifically used for leek (claimed).    ADVANTAGE - The present fertilizer utilizes biogas residue and biogas slurry, improves crop yield and quality and can inhibit the soil-borne disease.    DETAILED DESCRIPTION - A biological organic fertilizer specifically for leek, comprises: 400-500 pts. wt., preferably 450 pts. wt. dry rotten biogas residue; 80-120 pts. wt., preferably 100 pts. wt. grass carbon; 80-120 pts. wt., preferably 100 pts. wt. weathered coal; 40-60 pts. wt., preferably 60 pts. wt. molasses; 50-70 pts. wt., preferably 66 pts. wt. urea; 20-30 pts. wt., preferably 28 pts. wt. diammonium phosphate; 80-120 pts. wt., preferably 101 pts. wt. potassium sulfate; 51-137 pts. wt., preferably 79 pts. wt. kaolin; 800-1200 pts. wt., preferably 1000 pts. wt. biogas; not less than 100 million/g Bacillus megaterium; not less than 500 million/g Bacillus mucilaginosus; and not less than 1000 million/g Paenibacillus polymyxa. An INDEPENDENT CLAIM is included for the preparation of the biological organic fertilizer involving: uniformly mixing all raw materials, then putting in a disc granulating machine, spraying slurry, at the same time, introducing hot air, carrying out pelleting all components except a biogas slurry, granulating and sieving particles according to 3-5 mm, drying to obtain the granular fertilizer.
NOVELTY - A clopidogrel is prepared by brominating o-chlorophenyl acetic acid methyl ester using bromide/hydrogen peroxide or bromide/hydrogen peroxide adduct as brominating agent under acidic condition and with action of visible light or UV light to obtain alpha -bromo-o-chlorophenyl acetic acid methyl ester, and reacting with 4,5,6,7-tetrahydrothieno(3,2-c)pyridine hydrochloride to obtain racemic clopidogrel hydrochloride, or brominating o-chlorophenyl acetic acid methyl ester using bromide/hydrogen peroxide or bromide/hydrogen peroxide adduct as brominating agent under acidic condition.    USE - Preparation of clopidogrel for anti-platelet aggregation medicine.    ADVANTAGE - Preparation method is low in cost and environment-friendly, has mild reaction conditions, high brominating agent utilization rate, low energy consumption, and high yield, and avoids use of highly toxic bromination reagent, and product has high purity.    DETAILED DESCRIPTION - A clopidogrel is prepared by brominating o-chlorophenyl acetic acid methyl ester using bromide/hydrogen peroxide or bromide/hydrogen peroxide adduct as brominating agent under acidic condition and with action of visible light or UV light to obtain alpha -bromo-o-chlorophenyl acetic acid methyl ester, and reacting with 4,5,6,7-tetrahydrothieno(3,2-c)pyridine hydrochloride to obtain racemic clopidogrel hydrochloride, or brominating o-chlorophenyl acetic acid methyl ester using bromide/hydrogen peroxide or bromide/hydrogen peroxide adduct as brominating agent under acidic condition and with action of visible light or UV light to obtain alpha -bromo-o-chlorophenyl acetic acid methyl ester, performing condensation reaction with 2-thiopheneethylamine, salt splitting to obtain D-(+)- alpha -(2-thienylethylamino)- alpha -(2-chlorophenyl)acetate hydrochloride, and performing manich reaction with formaldehyde in which bromide is from hydrobromide, hydrobromic acid, or hydrobromic acid and hydrobromide mixture.
NOVELTY - An L-alanine is extracted by performing solid-liquid separation of L-alanine fermentation liquor to obtain supernatant, adding acid to adjust pH to 4.5-6, adding iron salt to obtain iron ion concentration of 7-18 mmol/L, adding 0.15-0.9 vol.% hydrogen peroxide, stirring at 40-80 degrees C, adding base to adjust pH to 7-8, optionally carrying out solid-liquid separation, adding 0.1-0.3% activated carbon at 50-80 degrees C while stirring, performing solid-liquid separation to remove activated carbon and to obtain decolorized solution, concentrating by evaporating under reduced pressure, and condensing.    USE - Extraction of L-alanine (claimed).    ADVANTAGE - The process is low cost and environment-friendly and improves product yield, and product has high light transmittance.    DETAILED DESCRIPTION - An L-alanine is extracted by performing solid-liquid separation of L-alanine fermentation liquor to obtain clear liquid, adding acid to adjust pH to 4.5-6, adding iron (Fe2+) salt to obtain Fe2+ ion concentration of 7-18 mmol/L, adding 0.15-0.9 vol.% hydrogen peroxide (H2O2), stirring at 40-80 degrees C, adding base to adjust pH to 7-8, optionally carrying out solid-liquid separation, adding 0.1-0.3% activated carbon at 50-80 degrees C while stirring, performing solid-liquid separation to remove activated carbon and to obtain decolorized solution, concentrating by evaporating under reduced pressure, condensing crystal, filtering, washing, and drying.
NOVELTY - Preparation of sancycline involves conversion of (4S,4aS,5aS,6S,12aS)-7-chloro-4-dimethylamino-3,6,10,12,12a-pentahydroxy-1,11-dioxo-1,4,4a,5,5a,6,11,12a-octahydro-naphthacene-2-carboxylic acid amide hydrochloride salt to sancycline in mixed solvent of alcohol and acid, under hydrogen environment, and in presence of catalyst. The alcohol is 1-6C alcohol. The acid is sulfuric acid, hydrobromic acid, methanesulfonic acid, 85% phosphoric acid, p-toluene sulfonic acid, and perchloric acid.    USE - For preparing sancycline (claimed).    ADVANTAGE - The preparation provides high yield and high purity, is simple process; recycles solvent and catalyst; is cost low; and is suitable for industrial production.
NOVELTY - Preparation of isoquinolin methanamide derivative (I) involves reacting aldehyde, 3-oxo-butyric acid ethyl ester and 4-hydroxy-chromen-2-one in presence of ammonia water as nitrogen source and reaction solvent in microwave, cooling and filtering to obtain filter cake, drying the filter cake by ethanol re-crystallization to obtain isoquinolin methanamide derivative (I).    USE - For preparation of isoquinolin methanamide derivative (claimed) used for synthesizing of medicine, dye, pesticide, food feed additive, antioxidant and chemical auxiliary agent.    ADVANTAGE - The method is one-pot method, recycles rest ammonia water, reduces reaction time and cost, improves reaction yield and economical efficiency, is environmental friendly, and reduces pollution to the environment.    DETAILED DESCRIPTION - Preparation of isoquinolin methanamide derivative of formula (I) involves reacting aldehyde of formula R-CHO, 3-oxo-butyric acid ethyl ester and 4-hydroxy-chromen-2-one in presence of ammonia water as nitrogen source and reaction solvent in microwave, cooling and filtering to obtain filter cake, drying the filter cake by ethanol re-crystallization to obtain isoquinolin methanamide derivative (I).    R=aryl (optionally substituted by methyl or nitro), naphthalene, thiophene, or furan ring.
NOVELTY - A (9S,13R,14S)-7,8-dehydrogenated-4-benzyloxy-3,7-dimethoxy-17-methyl-morphinan-6-ketone is demethylated to obtain demethylated intermediate. The demethylated intermediate and acetyl chloride are reacted to obtain (9S,13R,14S)-7,8-dehydro-4-benzyloxy-3,7-dimethoxy-17-acetyl-morphinan-6-one .    USE - Synthesis of (9S,13R,14S)-7,8-dehydro-4-benzyloxy-3,7-dimethoxy-17-acetyl-morphinan-6-one (claimed).    ADVANTAGE - The (9S,13R,14S)-7,8-dehydro-4-benzyloxy-3,7-dimethoxy-17-acetyl-morphinan-6-one is synthesized with high reaction selectivity and yield and less side reactions, by simple method.
NOVELTY - Preparation of tetrahydropyridine ketone derivative (I) involves reacting aromatic aldehyde (Ia), 5,5-dimethyl-cyclohexane-1,3-dione (IIa) and aromatic hydrazine hydrochloride (IIIa) in presence of an ion liquid (b) as catalyst by using ethanol as reaction solvent, under microwave condition, after finishing reaction, evaporating the solvent, washing with water and filtering, drying the filter cake and re-crystallizing with ethanol to obtain the tetrahydropyridine ketone derivative (I).    USE - For preparation of tetrahydropyridine ketone derivative (claimed) for treating breast cancer.    ADVANTAGE - The method has mild reaction condition, is simple for operation, reduces reaction time, recycles ion liquid catalyst, is environmental friendly, provides product having high yield and high purity.    DETAILED DESCRIPTION - Preparation of tetrahydropyridine ketone derivative of formula (I) involves reacting aromatic aldehyde of formula (Ia), 5,5-dimethyl-cyclohexane-1,3-dione (IIa) and aromatic hydrazine hydrochloride of formula (IIIa) in presence the ion liquid of formula (b) as catalyst by using ethanol as reaction solvent, under microwave condition, after finishing reaction, evaporating the solvent, washing with water and filtering, drying the filter cake and re-crystallizing with ethanol to obtain the tetrahydropyridine ketone derivative (I).    Y'=CF3SO3;    R1=hydrogen or methyl;    R2=hydrogen, chlorine, or nitro.
NOVELTY - Preparing horse acid involves mixing 2-((2-hydroxy-ethyl)-methyl-amino)-ethanol, 4-aminomethyl-benzoic acid and catalyst, heating at 70-100 degrees C in water, reacting for 2-5 hours at 60-100 degrees C, cooling to room temperature, filtering to obtain 4-((4-methyl-piperazin-1-yl)methyl)benzoic acid; and passing hydrogen chloride gas through solution of 4-((4-methyl-piperazin-1-yl) methyl) benzoic acid in organic solvent, stirring and dissolving, filtering, and separating out white solid to obtain horse acid i.e. 4-((4-methyl-piperazin-1-yl)methyl) benzoic acid dihydrochloride.    USE - For preparing horse acid (4-((4-methyl-piperazin-1-yl)methyl) benzoic acid dihydrochloride) (claimed) for preparing imatinib used as anti-tumour medicine.    ADVANTAGE - The method reduces reaction steps, is simple for operation, is easy to control, green and environmental friendly, and prepares product having high yield i.e. 95% and purity i.e. more than 99.5%.
NOVELTY - This utility model belongs to the technical field of chemical equipment, relates to a kind of oil-water separating solid kitchen waste and recycling organic liquid fertilizer, comprising a oil-water solid-liquid separation groove, impurity, crush tube, fermentation tank secondary waste water recycling pipeline, a lactic acid fermentation groove for a fermentation and liquid fertilizer for improving the quality and maturity of filter tank, the oil-water solid-liquid separation groove and the fermentation tank through a residual impurity, crush tube and waste water recycling pipe is connected with outlet of the fermentation tank is connected with the fermentation tank, the fermentation tank with filter tank. This utility model device in accordance with Chinese basic condition, improving the dealing with kitchen garbage, the kitchen garbage by microorganism and so on organic matter, improves the resource product value by the oil water gravity separation method.
NOVELTY - A kind of organic fertilizer fermenting-free turning device, comprising a data processing device, a temperature adjusting device, a temperature detecting device, a temperature adjusting device comprises a fan, a main blast pipe, a blast pipe, a buffer filter net cooling air and cooling pipe, the cooling pipe is provided with a gas hole and cooling air buffer filter net covered on the cooling pipe, a fan and a processing device is electrically connected with the main air outlet pipe of the fan is connected with the main pipe through the branch pipe and embedded in the organic material stack and covered with a cooling pipe for cooling air buffer filtering net, a temperature detecting device and cooling a relatively-fixed to the casing. A material and organic-free organic fertilizer fermenting pile-turning equipment for cooling air into the cooling tube and in the organic material stack by means of cold air buffer filter screen to dynamically adjust organic material stack in the stack the oxygen content of the inner part, so as to prevent the beneficial microorganism and fermentation bacteria die due to over-high temperature, so it does not need the operator in turning operation.
NOVELTY - Biogas fermentation nutrient soil is produced by cutting 1 m3 straw into small pieces of 10 cm long; adding small pieces of straw to a biogas digester and performing sealed fermentation for 25-30 days; removing residue from biogas digester and drying the residue; crushing the residue into 0.1-1 cm particles; and adding the particles with 50-60 kg soil, 5-6 kg nitrogen fertilizer, 4-5 kg potassium fertilizer, and 2-3 kg phosphate fertilizer and stirring, then spraying 40-50 kg water, spreading the mixed material to dry, and packaging into bags where each bag contains 2 kg nutrient soil.    USE - Method of producing biogas fermentation nutrient soil (claimed).    ADVANTAGE - The method involves liquid methane fermentation of straw stalks to degrade straw into small granular active molecules and avoid destruction of straw burning process on surface environment and the atmosphere.
NOVELTY - Humus, silicon and calcium preparation involves wetting rice husk as vegetable waste, and degrading and adapting material to be attacked by both fungi and bacteria. The treated material is processes by annelids, where the material is separated by screening to receive organic material such as silicon and calcium, and humus. The wetting of the plant material is performed by dipping the rice husk in a solution of water and caustic soda for one to ten days. The treated rice husk is washed with water and then immediately immersed in silicate aqueous solution, preferably sodium silicate.    USE - Method for preparing humus, silicon and calcium for use in fertilizer, food, medicine, and cosmetology (claimed).    ADVANTAGE - The method provides humus, silicon and calcium in a simple and eco-friendly manner.
NOVELTY - Manufacture of benzidine yellow G involves adding chlorine, water, hydrochloric acid and diclofenac, in nitrogen barrel, stirring, pulping, adding ice while stirring, reducing the resultant material liquid to 0 degrees C in the nitrogen barrel, adding sodium nitrite solution to nitrogen barrel, reacting the material liquid at 5 degrees C for 40-90 minutes, adding activated carbon, stirring, adding water to make the total volume of 1050-1150 L, diluting, adding turkey red oil, stirring for 1 minute or more, and suction filtering of diazo solution using cloth bag.    USE - Manufacture of benzidine yellow G (claimed).    ADVANTAGE - The method enables environmentally-friendly manufacture of benzidine yellow G, without self-dual diclofenac reaction.    DETAILED DESCRIPTION - Manufacture of benzidine yellow G involves adding chlorine, 650-750 kg water, 105-125 kg 30-35% hydrochloric acid and 60-80 kg diclofenac, in nitrogen barrel, stirring, pulping for 1 hour or more, adding ice while stirring, reducing the resultant material liquid to 0 degrees C in the nitrogen barrel, adding 38.4-39 kg 38-42% sodium nitrite solution to nitrogen barrel, reacting the material liquid at 5 degrees C for 40-90 minutes, adding 0.9-1.5 kg activated carbon, stirring at 5 degrees C for 3-10 minutes, adding water to make the total volume of 1050-1150 L, diluting by adding 9-11 times water, adding 0.3-0.7 kg turkey red oil, stirring for 1 minute or more, and suction filtering of diazo solution using cloth bag.
NOVELTY - System for treating forest waste green, comprises a fermentation tank, a green waste utilization system, a land system, a water supply system and a stable cover layer, where the treatment process comprises adding waste green into a fermentation tank, adding effective bacteria to ferment and decompose in the tank, adding edible plant fungus strain and earthworm and then covering using the land system, the water supply system, and then covering using stable cover layer.    USE - The system is useful for treating forest waste green (claimed) to produce organic fertilizer.    ADVANTAGE - The system can effectively treat the forest waste green, occupies small floor space and reduces water pollution and water resources in a low maintenance cost.
NOVELTY - A soybean protein bio-fermentation of organic fertilizer involves uniformly mixing organic fertilizer and bran having weight ratio of 1:10, to form ferment; adding ferment material, and then adding auxiliary material, mixing them uniformly, adding fermentation material, fermenting at 60-65 degrees C, and stacking to ferment for 6-8 days, where the auxiliary material includes livestock excrement, straw, and cassava slag.    USE - For soybean protein bio-fermentation of organic fertilizer (claimed).    ADVANTAGE - The method has short reaction time; provides fermented product having non-toxic, harmless, and no peculiar smell; does not have pollution to the environment; can save nutrient; improves organic matter content in the fertilizer, thus improve the utilization ratio of fertilizer.
NOVELTY - An 4-(4-methyl-piperazin-1-ylmethyl)-benzoic acid dihydrochloride is prepared by reacting p-methyl benzoic acid, N-methyl piperazine, solvent, and acid-binding agent to obtain acid-containing imatinib, removing N-methyl piperazine, acid-binding agent, and chloride salts by nanofiltration, and centrifuging.    USE - Preparation of 4-(4-methyl-piperazin-1-ylmethyl)-benzoic acid dihydrochloride (claimed).    ADVANTAGE - The preparation is simple, easy, recyclable, and environment-friendly and has cheap and easy to obtain raw material, low production cost, and low energy consumption, and product has high yield and purity.
NOVELTY - The utility model claims a kind of resource type bio-toilet, comprising closet bowl, fermentation tank, fermentation tank closet bowl is set at the lower part of the solid-liquid separator, a solid-liquid separator of excrement outlet connected with the fermentation device is provided with a stirring device, a stirring operation frequency of the device is as follows: a groove stirring device starting process each time a feeding back a stir, initial stirring device for a second level of the two back stirring and turning the stirring device for 6 + 0.5 for a second level of the two back stirring turning straight to the next of a fermenter. Excrement mixture stirring device is pushed to the discharging port of the fermentation tank, a primary fertilizer after a certain time. The whole fermentation process of the utility new-type does not need other energy consumption, there is no need for power or natural gas heating, it can convenient and effective treatment of dejecta, but also saves energy.
NOVELTY - The utility model relates to the technical field of producing amantadine hydrochloride, especially relates to one kind of hydrochloric acid adamantane amine in reaction kettle heating device, comprising an amination kettle, the raw material tank, a gas outlet, the amination reaction kettle is connected with the raw material tank, the amination reaction kettle in the kettle is provided with a stirring device, amination reaction kettle is provided with a gas outlet, wherein the amination reaction kettle is provided with a far infrared heating device, far infrared heating device replaces the original of heat conducting oil heating device, wherein the heating efficiency is improved, the heating speed is fast, reduces the energy consumption, reduces the production cost, the amination reaction speed, rapidly generating gas, the amination reaction kettle is provided with a long and thin structure, which can effectively reduce the gas material, and effectively reduces the gas environment pollution, improves the utilization rate of the raw material.
NOVELTY - The utility model relates to kitchen garbage and/or domestic garbage fast aerobic fermentation device, mainly provided with holes is cylindrical or box-type shell, a stirring device, a gas purifying device, a temperature sensor, an air dispersing pipe, a hot air heater, a blower, a controller and a water draining tank. This utility model shortens the time of fermentation, improves the fermentation speed and decrease the investment material fermentation and drying of the device, reduces the production cost of the fermenting and drying, improves the working efficiency, has good industrial practicability.
NOVELTY - A plurality of layer type aerobic fermentation storehouse the utility model relates to the living garbage and/or kitchen garbage, mainly composed of shell body, the fermentation chamber feeding port, glass viewing mirror, a thermometer or a detector, a stirrer, provided with holes of the left and right two pieces of material supporting plate, supporting plate to close or open the liquid pressure device, a spiral discharging device is composed of a multi-section fermenting chamber to ferment multiple layers, improves the utilization rate of the aerobic air, accelerates the speed of decomposed fermented material, improves the utilization rate of the device, small equipment occupation area. In particular, the fermentation materials are rolling under the action of a stirring device, a material is in loose state, the flow of hot air, fermenting material can quickly reach the best ferment temperature, accelerates the fermenting speed of the material, reduces the production cost of the fermentation, shortens the fermentation time, unit volume yield of the fermentation cabin is high, it has good industrial practicability.
NOVELTY - The utility model claims a kind of domestic garbage and/or kitchen garbage quick aerobic fermentation device, mainly composed of a cylindrical or a multiple-layer type fermenting chamber (39), an air heater (14), a feeding mechanism (6), a blower (13), a draining water storage tank (15) and gas purifying device (35) is composed of a multi-section fermenting chamber to ferment multiple layers, improves the utilization rate of the aerobic air, accelerates the speed of decomposed fermented material, improves the utilization rate of the device, small equipment occupation area. In particular, the fermentation materials are rolling under the action of a stirring device, a material is in loose state, the flow of hot air, fermenting material can quickly reach the best ferment temperature, accelerates the fermenting speed of the material, reduces the production cost of the fermentation, shortens the fermentation time, unit volume yield of the fermentation cabin is high, it has good industrial practicability.
NOVELTY - This utility model claims a composting system integrated device, comprising a fermentation tank, fermentation groove side is provided with changing groove track, the changing groove orbit is provided with changing machine, the fermentation groove use is provided with a track, the track is provided with a use and the upper part use rail and is further provided with a cloth pushing machine, the utility model technical solution of the invention can not be promoting blood circulation is not easy to recycle and utilize domestic waste quickly enough, and the pushing machine and the cloth wheel can realize the work controlling device of electrolysis bath, the labour can be saved.
NOVELTY - Humus liquid preparation involves degrading organic substance (1) which consists of tree, wood, grass or a dreg dipped in proper quantity of extremely strong vinegar acid (2). The vinegar acid is produced from carbon or charcoal. The organic material of wood type is also included from fish and shellfishes. The elution of the component of a humus liquid is controlled by infiltrating solid materials of zeolite, peat-moss, bark compost, a vermiculite or pearlite.    USE - Method for preparing humus liquid, such as humin, humic acid or fulvic acid for promoting bioactivity of animals and plants (claimed).    ADVANTAGE - The method prepares humus liquid in a simple and cost-effective manner with enhanced life. The prepared humus reduces hair damage, enhances hair straightening, stimulates germination, photosynthesis and metabolic, and improves disease resistant, drought resistance and activation of a vegetable enzyme by using natural mining resources in large quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the humus liquid preparation method.    Organic substance (1)    Vinegar acid (2)    Water tank (3)
NOVELTY - A tritylated alkyl aryl ether derivative, is new.    USE - Tritylated alkyl aryl ether derivative useful in the method of marking a petroleum hydrocarbon or a liquid biologically derived fuel (claimed).    ADVANTAGE - Tritylated alkyl aryl ether derivative efficiently marks a petroleum hydrocarbon or a liquid biologically derived fuel.    DETAILED DESCRIPTION - A tritylated alkyl aryl ether derivative having formula (Ph3C)mAr(R1)j(OR2)n, is new.    Ph=phenyl group;    Ar=aromatic ring system having 6-20C;    R1 and R2=1-18C alkyl or 4-18C heteroalkyl;    m=1 or 2;    j=1-4; and    n=1-3.    An INDEPENDENT CLAIM is included for marking a petroleum hydrocarbon or a liquid biologically derived fuel which involves adding to the petroleum hydrocarbon or liquid biologically derived fuel at least one compound having formula (Ph3C)mAr(R1)j(OR2)n present at a level of 0.01-20 ppm.
NOVELTY - Production line comprises a drying complex, a precipitator, a hammer mill, a stirrer, a granulator, a cooling column, a conveyor, rollers, a unit for packaging a finished product. The granulator is made in the form of a press granulator, which consists of a matrix with spinnerets that have at least one out of-plumb and/or a non-horizontal protrusion.    USE - The line is useful for the production of pellet and/or granular fertilizers from a residue of effluents (claimed).
NOVELTY - Processing substrates in the organic gaseous fuel and fertilizers, comprises: subjecting raw waste to a series of anaerobic treatment to produce biogas; aerobic treatment to obtain easily precipitating biosludge and oxygen-containing gas; separating into fractions to obtain a liquid and a solid fraction; and thermal utilization of the solid fraction to obtain ash and gaseous products, where the biosludge thermal energy is used to control temperature for the anaerobic treatment after its contact with the gaseous products of thermal recycling.    USE - The process is useful for processing substrates in the organic gaseous fuel and fertilizers.    DETAILED DESCRIPTION - Processing substrates in the organic gaseous fuel and fertilizers, comprises: subjecting raw waste to a series of anaerobic treatment to produce biogas; aerobic treatment to obtain easily precipitating biosludge and the oxygen-containing gas; separating into fractions to obtain a liquid and a solid fraction; and thermal utilization of the solid fraction to obtain ash and gaseous products, where the biosludge thermal energy is used to control temperature for the anaerobic treatment after its contact with the gaseous products of thermal recycling. The thermal recycling is carried out in the gasification mode with an oxygen-containing gas and the gaseous products to obtain a gas generator, for regulating the temperature and humidity of the anaerobic treatment of the solid fraction of the liquid thermal energy used biosludge fraction, which was then sequentially subjected to anaerobic treatment and additional stripping, and resulting ammonia water used for preparing organic fertilizer.
NOVELTY - This invention relates to an automatic organic cultivation structure, comprising at least a rack body assembly, at least a introducing connection pipe disposed on the rack body assembly, at least a cultivation device disposed with a connection element cooperatively actuated with the introducing connection pipe, and at least a driving element received in the cultivation device and connectingly actuated with the connection element. When the plant is placed on the carrying part, the operator can place the kitchen waste into the cultivation device; perform fermentation and storage after the kitchen waste is smashed; and finally introduce the processed kitchen waste to the plant by the driving element through the connection element and the introducing connection pipe, so as to achieve the practical objective of environmental protection, automation, and convenience in use.
NOVELTY - Insecticide comprises plant raw material chosen from 0.1-0.2% toosendanin, 0.6-0.8% matrine, 8-55% Cedrela sinensis extract, 0.2-0.5% flos daturae, 15-30% potassium chloride, and 0.1-0.2% Stemona.    USE - As insecticide.    ADVANTAGE - The insecticide does not cause any toxic effect to crop and vegetable, and causes minimal environment pollution.
NOVELTY - Preparing negative hydrogen ion product comprises placing calcium hydride or small particles of edible oil into anhydrous oxygen-free environment, carrying out ball milling, grinding calcium hydride to sub-micron particles and then coating on the surface of film to non-oxygen water and sieving to remove crude particles, separating and removing the redundant oil.    USE - The method is useful for preparing negative hydrogen ion product (claimed).    ADVANTAGE - The method simply, rapidly and economically prepares the negative hydrogen ion product in an eco-friendly manner with high purity, utilization rate and yield, and without toxicity.
NOVELTY - Preparing mink excrement biological organic fertilizer, comprises fermenting mink manure with Ascaris eggs and Escherichia coli at a temperature of 70-80 degrees C, carrying out enzymolysis to the fermented mixed auxiliary material, adding trace element and uniformly stirring, mixing the finished product and granulating, pelleting and drying the finished product.    USE - The method is useful for preparing mink excrement biological organic fertilizer (claimed).    ADVANTAGE - The fertilizer ensures fertility.
NOVELTY - This utility model claims a kind of livestock and poultry corpse epidemic prevention rapid flapping killing machine, wherein it comprises a stirring fermentation cylinder, wherein the stirring fermentation cylinder is provided with a transmission shaft, the transmission shaft is provided with a plurality of stirring crusher, stirring crusher crushing cutter is installed on the side of the transmission shaft is connected to the sieving device is composed of a discharge hole of the air outlet is set with a motor driving the stirring fermentation cylinder, the bottom of the stirring fermentation cylinder is provided with an electromagnetic heater, the top of the stirring fermentation cylinder is provided with a cover, stirring the fermentation cylinder to the upper part of the side wall is provided with a part of the feeding conveying device at the discharging end, the bottom of the stirring fermentation cylinder is provided with a discharging device, a discharging device. This utility model uses livestock and poultry corpse by quick processing, the livestock and poultry body eliminating base source and a farming production process and body in time, prevent loss caused by a disease, spoilage pollution environment, illegal operation harm the food safety; At the same time also to a livestock and poultry corpse, obtaining regenerated biological diesel oil with organic fertilizer source.
NOVELTY - The sludge aerobic composting method involves using sludge stirring tank, sludge dewatering pump, membrane sludge press filter, belt conveyor, sludge crushing and mixing machine, mixer, and transporting vehicle.    USE - Sludge aerobic composting method (claimed).    ADVANTAGE - The method economically and efficiently provides treated sludge with high quality, with reduced composting time even during winter and reduced floor area for fermentation chamber.
NOVELTY - Preparing bio-organic fertilizer, comprises preparing strain seed solution for preventing and treating root rot, preferably Bacillus subtilis solution as anti-root rot, fermenting at pH of 6.2-8.1 for 36-48 hours, and incubating at 24-37 degrees C.    USE - The fertilizer is useful for treating and preventing root rot of crop (claimed).    ADVANTAGE - The method utilizes domestic waste and ensures recycling of organic solid waste of pigs, cattle, and sheep.
NOVELTY - Biochemically treating tobacco disease residues, comprises crushing tobacco residue, classifying and adding into a fermentation machine, raising temperature to 80-110 degrees C for 4 hours, adding yeast as degradation bacteria to ferment at a temperature of 60 degrees C for 18 hours, adding soil beneficial bacteria, first-stirring at 40 degrees C for 1-2 hours, and discharging.    USE - The method is useful for biochemically treating tobacco residues, which is useful as fertilizer (claimed).    ADVANTAGE - The method treats tobacco residues to rapidly produce high-quality active organic fertilizer.
NOVELTY - Preparing organic nutrient soil using straw biogas residue comprises (a) discharging biogas residue from a biogas tank to a solid-liquid separation machine, carrying out solid liquid separation to obtain dehydrated residue having 55-65% water content, and (b) uniformly mixing dehydrated biogas residue, soil, wooden meal, organic fertilizer and inorganic fertilizer, stirring uniformly, feeding into a fermentation tank, sealing, and carrying out room temperature anaerobic fermentation for 15-25 days.    USE - The method is useful for preparing organic nutrient soil using straw biogas residue (claimed).    ADVANTAGE - The organic nutrient soil solves the problem of poor fertility, high amount of inorganic fertilizers and high cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for organic nutrient soil prepared by the above mentioned method.
NOVELTY - 1,1,1,4,4,4-hexafluoro-2-butene is prepared by reacting 1,1,1,4,4,4-hexafluoro-2,3-dichloro-2-butene with zinc powder in presence of solvent in which solvent is organic acid, inorganic acid, alcohol, amine, phenol, alkyl-substituted phenol, alkoxy-substituted phenol, ethanolamine, diethanolamine, or triethanolamine, organic acid is formic acid, acetic acid, propionic acid, butyric acid, valeric acid, benzoic acid, oxalic acid, malonic acid, glutaric acid, adipic acid, maleic acid, or fumaric acid and inorganic acid is hydrochloric acid and/or sulfuric acid.    USE - Preparation of 1,1,1,4,4,4-hexafluoro-2-butene (claimed).    ADVANTAGE - 1,1,1,4,4,4-hexafluoro-2-butene is easy to separate, and preparation is simple, low-cost, and environment-friendly and has high yield and selectivity, mild reaction, and fast response.    DETAILED DESCRIPTION - 1,1,1,4,4,4-hexafluoro-2-butene is prepared by reacting 1,1,1,4,4,4-hexafluoro-2,3-dichloro-2-butene with zinc powder in presence of solvent in which solvent is organic acid, inorganic acid, alcohol, amine, phenol, alkyl-substituted phenol, alkoxy-substituted phenol, ethanolamine, diethanolamine, or triethanolamine, organic acid is formic acid, acetic acid, propionic acid, butyric acid, valeric acid, benzoic acid, oxalic acid, malonic acid, glutaric acid, adipic acid, maleic acid, or fumaric acid, inorganic acid is hydrochloric acid and/or sulfuric acid, alcohol is methanol, ethanol, propanol, isopropanol, butanol, ethylene glycol, glycerol, cyclohexanol, or benzyl alcohol, and amine is dimethylamine, ethylamine, N-propylamine, N-butylamine, cyclohexylamine, ethylenediamine, diisopropylamine, benzylamine, aniline, or alkyl-substituted aniline.
NOVELTY - Preparing Tagalsin C having anti-tumor activity involves: (1) adding Tagalsin E and tertiary butyl alcohol potassium and anhydrous tetrahydrofuran into reaction container; evacuating the vessel with oxygen at -15 degrees C for 10 hours, to obtain reaction product (p1); (2) reacting Tagalsin G and anhydrous dimethyl sulfoxide in presence of palladium acetate and oxygen for 24 hours at 60 degrees C to obtain reaction product (p2); and (3) extracting the products (p1, p2) using petroleum ether and ethyl acetate, in normal phase silica gel column chromatography, decompressing and concentrating.    USE - For treating tumor (claimed).    ADVANTAGE - The method requires fewer steps, provides Tagalsin C with high yield and green and environment-friendly.
NOVELTY - 7-chloro-1-((2-methyl-4-nitrophenyl)carbonyl)-2,3,4,5-tetrahydro-1H-1-benzazepin-5-one as Tolvaptan intermediate is reduced in concentrated sulfuric acid in the presence of a metal reducing agent and a solvent, and 1-(4-amino-2-methyl-benzoyl)-7-chloro-5-oxo-2,3,4,5-tetrahydropyranyl ether 1H-1-benzazepine compound is produced.    USE - Manufacture of amino methyl benzoyl-7-chloro-5-oxo-tetrahydropyranyl ether 1H-1-benzazepine compound (claimed).    ADVANTAGE - The amino methyl benzoyl-7-chloro-5-oxo-tetrahydropyranyl ether 1H-1-benzazepine compound is produced at high yield by simple method without affecting the environment.
NOVELTY - Purifying artesunate comprises sequentially adding chloroform, dihydroartemisinin, succinic anhydride and triethylamine into a reaction tank and reacting by stirring, transferring into separating funnel, adding purified water and extracting many times and filtering the reaction solution, concentrating by evaporation, adding equal volume of petroleum ether into the concentrated filtrate, stirring, crystallizing, centrifuging and filtering, adding methanol into crude artesunate, stirring, adding purified water and stirring until all crystals precipitate out, centrifuging, filtering and drying.    USE - The method is useful for purifying artesunate (claimed).    ADVANTAGE - The method is simple, economical, environmentally friendly and consumes less energy; has shortened reaction time and produces more than 93% yield having more than 99%,purity, and recovers the solvent.    DETAILED DESCRIPTION - Purifying artesunate comprises: (i) sequentially adding chloroform, dihydroartemisinin, succinic anhydride and triethylamine into a reaction tank and reacting by stirring for 0.5-2 hours under room temperature, detecting the reaction via thin-layer chromatography, and adding excess acid to stop the reaction; (ii) transferring the reaction mixture into a separating funnel, adding equal amount of purified water and extracting many times until the aqueous layer is clear, and filtering the reaction solution; (iii) concentrating the filtrate to 1/20-1/25 of its original volume by evaporation; (iv) adding equal volume of petroleum ether into the concentrated filtrate, stirring uniformly, allowing it to stand for 4-6 minutes for crystallization, centrifuging and filtering to obtain crude artesunate filter cake; (v) adding methanol into crude artesunate, stirring for complete dissolution under room temperature, adding purified water under stirring condition until all crystals precipitate out, centrifuging and filtering; and (vi) drying the artesunate crystals.
NOVELTY - This utility model claims an excreta organic fertilizer water flushing device, comprising a ball valve main body structure, a bearing bench, a barrel and is tightly combined with the person sitting defecation is matched with an elliptic shape and the upper part shell is an opening surface of the upper part is provided with an installation hole and is connected with a barrel opening of the annular opening to the lower part of the outer exhaust pipe joint, a lower half, the upper and lower shell with the shell connection part are uniformly distributed around the screw, fastened to holding ball rotating core with an opening through the opening of the main body to form a bearing space, the rotating shaft and the shaft extends through the two ends of rotate gear pair position with the inner cavity and the bottom liquid pit in ball valve, wherein the transit of spherical core, bearing the opening face upwards, bearing human manure urine and peculiar smell is discharged from the exhaust port, a bearing of steering opening downwards, manure urine automatic tipping, falls to a storage barrel, an outer spherical surface to upper part sealing hole preventing peculiar smell leaking main body is suitable for making water-saving organic fertilizer reducing and a toilet.
NOVELTY - This utility model claims a kind of domestic garbage three separate ventilation air cap. Using the gravity of the liquid and the solid, the penetrating fluid and which carries the solid particles into the collecting groove through the ventilation hole, the solid and settling final in collecting groove, the filtrate accumulated to a certain degree, the overflow hole to the percolate guide discharging channel, at the same time, the gas enters into the air cap through the air inlet hole, the stack through the ventilation hole. Ventilation air cap on the clapboard is made of steel structure, a clamp slot is fixed air floor, the design form is easy to change. This utility model is advantaged in simple structure, easy manufacturing process, using a structure easy to change, convenient cleaning and so on, realizing the gas and liquid of the domestic garbage ventilation system, separating the slag.
NOVELTY - This utility model claims a method for producing a special medlar fertilizer is new, the device belongs to the field of organic fertilizer field, comprising a fermentation tank, a fermenting tank, a crusher, a crusher, a mixing tank, wherein the fermentation groove is provided with a manure inlet, inlet, inlet bacteria, organic phosphorus decomposing bacteria inlet, inlet phosphorus bacteria, potassium bacteria inlet, root inlet, a fermentation tank is provided with a first conveyor to crusher, the fermentation tank is provided with a river mud inlet, fruit dreg inlet, inlet, monosodium glutamate dreg inlet, organic fertilizer fermenting agent inlet, the upper part is provided with a crusher inlet corn straw and peanut shell inlet, inlet, inlet of monoammonium phosphate, potassium sulphate inlet, the amino acid chelating microelement inlet, the humic acid chelating microelement inlet, between the fermenting tank is provided with a second conveyor, a fermenting tank is provided with a third conveyor to crusher, between the crusher to the mixing pool is provided with a fourth conveyor, crusher to mixing tank is provided with a fifth conveyer.
NOVELTY - This utility model claims a kind of production plant honeysuckle special base fertilizer for new device, belonging to the field of organic fertilizer, comprising a crusher, a fermenting tank, a crusher, mixing tank, wherein it is as follows: the upper part is provided with a crusher inlet manure, pig manure inlet, cow dung inlet, river mud inlet, a leaf inlet, inlet of oilseed rape straw, wheat bran inlet, colza cake inlet, inlet diammonium phosphate, potassium sulphate inlet, the humic acid chelating microelement inlet of grinder of the fermentation pool is provided with a conveyor, a mixing tank is provided with a conveyor, the fermentation tank is provided with plant ash inlet, organic fertilizer fermenting agent inlet, a deodorant organic fertilizer inlet, a fermenting tank is provided with a third conveyor to crusher, crusher to mixing tank is provided with a fourth conveyor, the mixing tank is provided with a finished product outlet.
NOVELTY - Garden greening waste treatment for water saving system, comprising a fermentation of a spraying device, rainwater and waste liquid collecting device. The upper part pipe comprises fermentation with a fermenting tank for spraying device and a plurality of atomizing nozzle is set along the length direction of the fermentation tank and so on space, connected with the atomizing spray head is provided with a total switch and control switch, water and the waste liquid collecting device comprises a water storage tank, a waste liquid conveying groove, the rain collecting-and-conveying groove, the water collecting groove is set at the bottom of the fermenting tank along the length direction, the cross section is V-shaped, and the waste liquid conveying groove is connected with the waste liquid conveying direction, conveying the waste liquid is gradually reduced to the bottom surface of the height continuous groove, rainwater collecting-and-conveying groove is set at outer edge of the roof, rain water along the conveying direction, wherein the inner bottom surface of the continuous height is gradually reduced, and the water storage tank is provided with a cover plate. Using the system, which not only can reduce the water cost, but also makes full use of waste liquid nutrient for plant afforestation irrigation, it is economic and environment-friendly.
NOVELTY - An aerobic fermentation unit comprises base (1), detachable bottom wall plate (13), vertical fixing rod (2), detachable front wall plate (3), two side wall plates (4,6), rear wall plate (5), detachable top cover (7), vent holes (8) and air outlet hole (9).    USE - Aerobic fermentation unit for composting organic waste.    ADVANTAGE - The unit can be adapted to different fermentation processes.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of aerobic fermentation unit.    Base (1)    Vertical fixing rod (2)    Detachable front wall plate (3)    Side wall plate (4)    Rear wall plate (5)    Side wall plate (6)    Detachable top cover (7)    Vent holes (8)    Air outlet hole (9)    Detachable bottom wall plate (13)
NOVELTY - Bio-organic fertilizer comprises 0.1-0.2 pt. wt.Aschersonia powder, 14-25 pts. wt. lai cake, 25-40 pts. wt. chicken manure, 30-40 pts. wt. rice bran, 1-2 pts. wt. amino acids, 0.01-0.02 pt. wt. Rhodococcus powder, 0.01-0.02 pt. wt. Chinese steamed stuffed buns, 0.01-0.02 pt. wt.Escherichia coli, 0.01-0.02 pt. wt. Bacillus subtilis powder and 1-2 pts. wt. microelement fertilizer.    USE - Bio-organic fertilizer used for generating organic pollutant in soil and producing active substances to stimulate crop growth.
NOVELTY - Preparation of slow-release fertilizer comprises carbonizing with straw, animal excrement, rice, and livestock waste as raw material at low temperature.    USE - Method of preparation of slow-release fertilizer (claimed).    ADVANTAGE - The method saves resource, has no pollution, high yield and low cost, and is environment-friendly production.
NOVELTY - A natural soil conditioner is prepared by mixing acetobacter seed liquid culture medium and medicinal plants or agricultural crop straw, crushing, sieving through 20 mesh sieve to obtain solid fermentation substrate, mixing with wood vinegar at weight ratio of 1:0.07-0.1, adding magnesium phosphate and trace element, and drying to room temperature.    USE - Method for preparation of natural soil conditioner (claimed).    ADVANTAGE - The method is simple, convenient, and environment-friendly, and has soil fertility effects and low cost. The conditioner improves quality of fertilizers, soil fertility, crop quality and efficacy, and promotes plant growth.
NOVELTY - Preparation of sitafloxacin intermediate (I) comprises dissolving sitafloxacin-containing compound (II) in polar solvent, reacting with Lewis base, monitoring reaction through thin layer chromatography until reaction is complete, and removing solvent.    USE - Method for preparation of sitafloxacin intermediate (I) used for pharmaceutical composition (claimed).    ADVANTAGE - The method is simple, easy to handle, and very suitable for large-scale industrial production, has high yield, and low cost, improves dissolution effect of product and bioavailability, and enhances efficiency.    DETAILED DESCRIPTION - Preparation of sitafloxacin intermediate of formula (I) comprises dissolving sitafloxacin-containing compound of formula (II) in polar solvent, reacting with Lewis base, monitoring reaction through thin layer chromatography until reaction is complete, and removing solvent.    R=H or halo.    An INDEPENDENT CLAIM is included for preparation of pharmaceutical composition by adding compound (I) to different pharmaceutical carrier and/or excipient.
NOVELTY - A drospirenone intermediate is new.    USE - A drospirenone intermediate (claimed).    ADVANTAGE - Preparation process is simple and environment-friendly, has easy operation, and does not need heavy metal and toxic reagent, and product has high purity.    DETAILED DESCRIPTION - A drospirenone intermediate of formula (I-a) is new.    R=H, Li, Na, K, one half Mg, one half Ca, NH4, CH3, CH2CH3, (CH2)2CH3, CH(CH3)2, (CH2)3CH3, CH2CH(CH3)2, or CH(CH3)3.    An INDEPENDENT CLAIM is included for preparation of drospirenone intermediate of formula (I).
NOVELTY - A 5-(4-(4-(5-cyano-3-indolyl)-butyl)-1-piperazinyl) benzofuran-2-carboxylic acid ethyl ester (vera trazodone intermediate) is synthesized by adding 3-(4-chloro-butyl)-5-cyano-indole with anhydrous catalyst to solvent under nitrogen, reflux heating with stirring, adding 5-(piperazin-1-yl) benzofuran-2-carboxylic acid ethyl ester and base, reacting for 4-6 hours at 80-110 degrees C, cooling to room temperature, pouring slowly with stirring to precipitate solid base aqueous solution, stirring for 0.5-2 hours, filtering, washing, and drying to obtain crude product.    USE - Synthesis of 5-(4-(4-(5-cyano-3-indolyl)-butyl)-1-piperazinyl) benzofuran-2-carboxylic acid ethyl ester (vera trazodone intermediate) for medicines (claimed).    ADVANTAGE - Preparation process is low-cost, environment-friendly, safe in operation, high in yield and purity, good in quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a liquid phase chromatograph of vera trazodone intermediate.
NOVELTY - A tenofovir disoproxil fumarate is synthesized by performing condensation reaction of tenofovir and/or tenofovir monohydrate and chloromethyl isopropyl carbonate in the presence of dehydrating agent which is anhydrous calcium chloride, anhydrous calcium oxide, anhydrous potassium carbonate, anhydrous sodium carbonate, anhydrous magnesium sulfate, anhydrous sodium sulfate, and/or anhydrous calcium sulfate.    USE - Synthesis of tenofovir disoproxil fumarate used for making HIV-resisting medicine.    ADVANTAGE - Process is simple, environment-friendly, has low cost, high purity, and high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of synthesis of tenofovir disoproxil fumarate. (Drawing includes non-English language text).
NOVELTY - A high temperature degrading bacterium, which is Geobacillus HN-5 strain, deposited under CGMCC NO. 5852, is new.    USE - The high temperature degrading bacterium is useful for producing cellulase, amylase, and protease; promoting compost; improving quality of compost; and for decomposing at 18-63.5 degrees C (all claimed).    ADVANTAGE - The high temperature degrading bacterium provides rapid compost decomposition at high temperature.
NOVELTY - A low temperature resistant cellulose degrading bacterium, specifically Pseudomonas sp. B6-15 strain, deposited under CGMCC NO. 5851, is new.    USE - The low temperature resistant cellulose degrading bacterium is useful for producing cellulase; and for promoting composting by raising temperature to 15-20 degrees C (all claimed).    ADVANTAGE - The low temperature resistant cellulose degrading bacterium is provided for high-efficient degradation of cellulose.
NOVELTY - Urban agricultural wastes are recycled by collecting vegetable residue and animal residue and spraying with clean water to remove mud; adding water in a container and heating, adding vegetable residue in the container for blanching, then sterilizing and drying, and crushing the vegetable residue to be used as plant protein feed or organic fertilizer; adding animal residue into the container for blanching, removing blood dirt and scum, high temperature stewing for 1-2 hours, sterilizing and drying, and crushing to be used as animal protein feed or organic fertilizer.    USE - Method for recycling urban agricultural wastes (claimed).    ADVANTAGE - The method can recover remainder of original nutrients in agricultural waste at low cost and with easy operation.    DETAILED DESCRIPTION - Recycling urban agricultural wastes comprises:    (A) collecting vegetable residue and animal residue and spraying with clean water to remove mud;    (B) adding water in a container and heating, then adding vegetable residue in the container for blanching, and discharging water to obtain vegetable residue having water content of 50-60 wt.%;    (C) putting vegetable residue into a tunnel microwave dryer for sterilizing and drying to water content of less than or equal to 12 wt.%, and then crushing the vegetable residue to be used as plant protein feed or organic fertilizer;    (D) adding animal residue into the container for blanching, removing blood dirt and scum, then high temperature stewing for 1-2 hours, and discharging water to obtain animal residue having water content of less than or equal to 40 wt.%; and    (E) sterilizing and drying the animal residue in a tunnel dryer to water content of 12 wt.%, and then crushing to be used as animal protein feed or organic fertilizer.
NOVELTY - An ecological odorless organic fertilizer comprises 24-51 wt.% sheep manure, 11-16 wt.% corn flour, 17-23 wt.% straw, 6-11 wt.% plant ash, 8-13 wt.% soybean meal, 4-7 wt.% humic acid and 3-6 wt.% bacterial strain.    USE - Ecological odorless organic fertilizer used for flowers and potted plants.    ADVANTAGE - The organic fertilizer has high production efficiency, contains enough nutrients and does not destroy the soil structure.
NOVELTY - Organic fertilizer with effective microorganism bacteria comprises 54-56 wt.% rabbit manure, 14-16 wt.% chicken manure, 19-21 wt.% chaff, 4-6 wt.% soil, 0.5-2.5 wt.% effective microorganism bacteria, 0.5-1.5 wt.% sugar and 2-4% traditional Chinese medicine additive.    USE - Organic fertilizer with effective microorganism bacteria used for improving soil fertility.
NOVELTY - Efficient bio-organic fertilizer comprises 70 pts. wt. dry fermented rabbit dung, 70 pts. wt. fresh beaver rabbit excrement mixed with fermentation bacteria powder. Fermentation bacteria powder is composed of 1 wt.% fresh rabbit dung, 11 pts. wt. urea, 10 pts. wt. monoammonium phosphate, 11 pts. wt. potassium sulfate, 1 pt. wt. dolomite powder, 0.5 pt. wt. borax, 0.2 pt. wt. copper, 0.1 pt. wt. zinc sulfate, 0.2 pt. wt. manganese sulfate and 0.1 pt. wt. ammonium sulfate. The powder further comprises photosynthetic bacteria.    USE - Efficient bio-organic fertilizer.    DETAILED DESCRIPTION - Efficient bio-organic fertilizer comprises 70 pts. wt. dry fermented rabbit dung, 70 pts. wt. fresh beaver rabbit excrement mixed with fermentation bacteria powder. Fermentation bacteria powder is composed of 1 wt.% fresh rabbit dung fermented for 15-20 days at 55-70 degrees C, 11 pts. wt. urea, 10 pts. wt. monoammonium phosphate, 11 pts. wt. potassium sulfate, 1 pt. wt. dolomite powder, 0.5 pt. wt. borax, 0.2 pt. wt. copper, 0.1 pt. wt. zinc sulfate, 0.2 pt. wt. manganese sulfate and 0.1 pt. wt. ammonium sulfate. The powder further comprises photosynthetic bacteria containing 0.67 pt. wt. flour, 0.13 pt. wt. brown sugar, 0.2 pt. wt. aqueous solution of photosynthetic bacteria and 0.2 pt. wt. photosynthetic bacteria liquid. An INDEPENDENT CLAIM is included for preparation of efficient bio-organic fertilizer comprising mixing dry fermented rabbit dung with fermentation bacteria powder, crushing, sieving, mixing with various ingredients, extruding, hot air drying, sieving, spraying at temperatures below 60 degrees C and cooling.
NOVELTY - Agricultural green microbial pesticide comprises Bdellovibrio powder, Escherichia coli powder, Chinese Ephedra, ginger, agrimony, cocklebur fruit, pomegranate rind, folium artemisiae argyi, cordate houttuynia, common andrographis herb, Cannabis, Chloranthus, Chrysanthemum, tobacco, pokeweed, dandelion, leech, penetrating agent, potentiating agent, hairyvein agrimony, Euphorbia, Chinaberry fruit, and water.    USE - Used as an agricultural green microbial pesticide.    ADVANTAGE - The pesticide is environmentally friendly; does not produce secondary toxicity, residue, and pollution; and maintains ecological balance.    DETAILED DESCRIPTION - Agricultural green microbe pesticide comprises 1-3 pts. wt. Bdellovibrio powder, 1-3 pts. wt. Escherichia coli powder, 8-12 pts. wt. Chinese Ephedra, 1-2.5 pts. wt. ginger, 2.5-3.5 pts. wt. agrimony, 20-35 pts. wt. cocklebur fruit, 30-40 pts. wt. pomegranate rind, 1-3 pts. wt. folium artemisiae argyi, 11-21 pts. wt. cordate houttuynia, 9-16 pts. wt. common andrographis herb, 3-8 pts. wt. Cannabis, 7-9 pts. wt. Chloranthus, 9-13 pts. wt. Chrysanthemum, 2-5 pts. wt. tobacco, 3-8 pts. wt. pokeweed, 7-12 pts. wt. dandelion, 11-13 pts. wt. leech, 10-15 pts. wt. penetrating agent, 1-10 pts. wt. potentiating agent, 3-8 pts. wt. hairyvein agrimony, 7-9 pts. wt. Euphorbia, 80-120 pts. wt. Chinaberry fruit, and 100 pts. wt. water.
NOVELTY - The system has a raw material storage tank connected with an efficient STAIC anaerobic reactor. A biological film filter is fixed with a back washing tank and a greening and ecological bed. A separating device is provided with an annular water tank that is fixed with a power system unit and a rotary screen. The power system unit is fixed with a hook and a suspension discharging pipe. The washing tank is provided with a feeding pipe and a feeding tank. A marsh gas collecting rod is fixed with a filter plate that is fixed on a top block. A liquid groove is matched with a liquid storage tank.    USE - Domestic rubbish breeding waste water anaerobic treatment biogas fertilizing system.    ADVANTAGE - The system generates clean energy marsh gas and biogas, and reduces sanitary biogas residue fertilizer wastage rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a domestic rubbish breeding waste water anaerobic treatment biogas fertilizing system.'(Drawing includes non-English language text)'
NOVELTY - A boron-rich biological organic fertilizer comprises 8 pts. wt. swine manure, 1 pt. wt. straw and 0.25-0.75 pts. wt. boron sludge. Swine manure has moisture content of 70-80%. Straw length is 2-5 cm.    USE - Boron-rich biological organic fertilizer for utilizing boron-rich waste.    ADVANTAGE - The fertilizer is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of boron-rich biological organic fertilizer comprising taking pig manure, straw, and boron sludge, mixing, adjusting carbon-nitrogen ratio to 20-35:1, adjusting water content to 50-65%, charging into compost tank with height of 0.8-1 m, adding 5 cm of mixture, adjusting pH value to 8-9, composting for 50-60 days, drying to moisture content of 20-30%, and sieving through 20-mesh sieve.
NOVELTY - The method involves containing components such as 1-2 pts. wt. rice bran, 20-40 pts. wt. brown sugar, 2-5 pts. wt. diammonium phosphate, 2-5 pts. wt. potassium hydrogen livestock manure, 2-5 parts pts. wt. ferrous sulfate and 25-60 pts. wt. rice powder.    USE - Soil granule structure promoting method.    ADVANTAGE - The method enables improving survival and propagation activity of the earthworm in the soil and granule structure of the soil.
NOVELTY - The utility model claims a kind of using solar energy for producing bio-organic fertilizer by fermenting device, the device is composed of a box body, a solar focusing heat collector, a fermenting container parts, box body is made of light heat preservation material is made of sealed box body is provided with a solar heat collector on the body, the connecting pipe and the box is set in the S-shaped heating circulating pipe is provided with a fermentation container in the box body, the fermentation container is movable box body, is set in the inner cavity of the box body of the biological fertilizer raw material. Comprising collecting solar energy and biological fermentation as a whole, the production period is short, effect is good and an ozone-free, no environmental pollution, can effectively improve the agricultural production environment, and improves the quality of the crop product.
NOVELTY - Treating large farm animal waste comprises collecting a farm livestock manure by septic tank fermentation process; sewage drainage and irrigation; sending septic tank fermentation manure extract to the dehydration process; sending the feces into the centrifuge with a water content of 20%, and dehydrating; drying and dehydrating the separated feces to dry till the water content is 5%; crushing the feces and the dried feces; taking the crushed feces sampling in the assay; mixing feces ingredients; and packaging the feces ecological fertilizer.    USE - Method for treating large farm animal waste (claimed).    ADVANTAGE - The method is environment-friendly, safe and reliable, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for treating large farm animal waste comprising a septic tank (1), a sewage pump (2), a hoisting machine (3), a centrifuge (4), a dryer (5), a crusher (6), a storage hopper (7), a stirrer (8) and packaging machine (9).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of an apparatus for treating large farm animal waste (Drawing includes non-English language text).    Septic tank (1)    Sewage pump (2)    Hoisting machine (3)    Centrifuge (4)    Dryer (5)    Crusher (6)    Storage hopper (7)    Stirrer (8)    Packaging machine (9)
NOVELTY - Biofertilizer comprises 0.1-0.2 pt. wt. fermented bacteria, 0.1-0.2 pt. wt. bacteriophage powder, 0.1-0.2 pt. Oceanospirillales powder, 0.1-0.2 pt. wt. Beauveria bassiana powder, 0.1-0.2 pt. wt. Metarhizium anisopliae powder, 20-35 pts. wt. pig manure, 0.01-0.02 pt. wt. trace elements, 5-9 pts. wt. sodium dihydrogen phosphate, 2-7 pts. wt. disodium hydrogen phosphate, 3-8 pts. wt. sodium tripolyphosphate bran, 4-8 pts. wt. wheat bran, 2-7 pts. wt. manganese sulfate, 1-4 pts. wt. zinc sulfate and 15-25 pts. wt. urea.    USE - Biofertilizer used for increasing bacterial content of soil (claimed), improving immunity of plants, promoting plant growth and inhibiting bacterial growth.
NOVELTY - Organic agricultural fertilizer comprises 0.1-0.2 pt. wt. Aschersonia powder, 15-25 pts. wt. pigweed, 35-40 pts. wt. chicken manure, 4-9 pts. wt. vermicompost, 8-13 pts. wt. goosefoot, 5-9 pts. wt. wheat bran, 3-7 pts. wt. potato, 1-3 pts. wt. sucrose, 1-7 pts. wt. agar, 70-95 pts. wt. corn stover, 55-75 pts. wt. bean straw, 25-35 pts. wt. potato straw, 1-8 pts. wt. rock phosphate powder and 2-7 pts. wt. oyster shell powder.    USE - Organic agricultural fertilizer used for promoting plant growth.
NOVELTY - Pleiotropic microbial organic fertilizer comprises 30-55 pts. wt. chicken manure, 25-35 pts. wt. rice bran, 34-46 pts. wt. wheat bran, 10-24 pts. wt. potato, 5-9 pts. wt. sucrose, 9-15 pts. wt. agar, 3-8 pts. wt. phosphate rock, 1-4 pts. wt. ammonium dihydrogen phosphate, 1-3 pts. wt. sodium acid pyrophosphate, 0.1-0.3 pt. wt. Azotobacter powder, 0.1-0.3 pt. wt. phosphobacteria powder, 0.1-0.3 pts. wt. fungus root powder, 15-35 pts. wt. soybean straw and 10-25 pts. wt. potato straw.    USE - Pleiotropic microbial organic fertilizer used for reducing pest reproduction and treating Fusarium wilt, rust blight, Verticillium wilt and root rot.
NOVELTY - An organic biological composite fertilizer comprises 35-45 pts. wt. chicken manure, 10-15 pts. wt. sweet potato powder, 20-35 pts. wt. peat, 9-16 pts. wt. calcium superphosphate, 7-10 pts. wt. potassium sulfate, 1-6 pts. wt. nitric acid, 2-6 pts. wt. magnesium sulfate, 2-6 pts. wt. sodium chloride, 0.1-0.2 pt. wt. Bacillus powder, 35-45 pts. wt. rice stalk, 30-40 pts. wt. corn, 0.1-0.2 pt. wt. abamectin, 1-6 pts. wt. lotus root powder, 2-6 pts. wt. potassium dihydrogen phosphate, 1-2 pts. wt. sodium nitrophenolate, 1-2 pts. wt. naphthalene acetic acid and 1-2 pts. wt. humic acid.    USE - Organic biological composite fertilizer.    ADVANTAGE - The environment-friendly composite fertilizer has high content of nutrients.
NOVELTY - A green agricultural biological composite fertilizer comprises 4-9 pts. wt. phosphate rock, 8-12 pts. wt. potassium mineral powder, 15-25 pts. wt. limestone powder, 24-35 pts. wt. peat powder, 0.01-0.02 pt. wt. Rhodococcus powder, 0.01-0.02 pt. wt. steamed stuffed bun bacteria powder, 0.01-0.02 pt. wt. Escherichia coli powder, 0.01-0.02 pt. wt. Bacillus subtilis powder, 14-25 pts. wt. pigweed cake, 25-35 pts. wt. chicken manure, 14-23 pts. wt. rice bran and 1-2 pts. wt. rare earth fertilizer.    USE - Green agricultural biological composite fertilizer.    ADVANTAGE - The composite fertilizer is convenient and simple to prepare. It has high content of viable bacteria, thus improving quality of soil to obtain high crop yield.
NOVELTY - A microbial fertilizer comprises 50-90 pts. wt. livestock manure, 4-9 pts. wt. sodium dihydrogen phosphate, 5-6 pts. wt. disodium hydrogen phosphate, 6-15 pts. wt. sodium tripolyphosphate, 4-9 pts. wt. earthworm manure, 8-13 pts. wt. pigweed cake, 40-55 pts. wt. chicken manure, 15-35 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 14-24 pts. wt. bean straw, 5-9 pts. wt. potato straw, 0.1-0.3 pt. wt. Lactobacillus powder, 0.1-0.4 pt. wt. nitrification bacteria powder and 0.1-0.2 pt. wt. Rhizobium powder.    USE - Microbial fertilizer.    ADVANTAGE - The fertilizer has balanced nutrition, thus improving organic matter content of soil.
NOVELTY - An agricultural crop yield green microbial fertilizer comprises phosphate rock, potassium ore, stone powder, peat powder, potassium oxide, Aeromonas powder, Candida powder, potassium ore, stone powder, peat powder, diammonium phosphate, ammonium dihydrogen phosphate, Azotobacter, phosphobacteria, potassium bacteria, chicken, rice husk powder, straw, and urea.    USE - Agricultural crop yield green microbial fertilizer.    ADVANTAGE - The fertilizer has strong resistance, high level of viable cells and variety of enzymes, and high fertilizer efficiency and yield, and improves soil bacteria function, crop quality, and nitrogen, phosphorus, and potassium utilization.    DETAILED DESCRIPTION - An agricultural crop yield green microbial fertilizer comprises 4-9 pts. wt. phosphate rock, 8-12 pts. wt. potassium ore, 5-25 pts. wt. stone powder, 24-35 pts. wt. peat powder, 1-6 pts. wt. potassium oxide, 0.01-0.02 pts. wt. Aeromonas powder, 0.01-0.02 pts. wt. Candida powder, 4-8 pts. wt. potassium ore, 5-9 pts. wt. stone powder, 6-12 pts. wt. peat powder, 4-6 pts. wt. diammonium phosphate, 3-7 pts. wt. ammonium dihydrogen phosphate, 0.01-0.02 pts. wt. Azotobacter, 0.01-0.02 pts. wt. phosphobacteria, 0.01-0.02 pts. wt. potassium bacteria, 45-50 pts. wt. chicken manure, 25-35 pts. wt. rice husk powder, 45-60 pts. wt. straw, and 10-15 pts. wt. urea.
NOVELTY - A biological compound fertilizer comprises chicken manure, rice bran, wheat bran, potato, sugar, agar, phosphate rock, calcium dihydrogen phosphate, calcium dihydrogen phosphate, phosphate, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, Verticillium powder, Bacillus thuringiensis powder, Aschersonia powder, caterpillar fungus powder, cortex fraxini, and radix stemonae.    USE - Biological compound fertilizer used for maintaining agricultural ecological balance (claimed).    ADVANTAGE - The fertilizer can effectively prevent underground pests, reduces pest reproduction rate, drives off soil pests, and has antiblight, fusarium wilt, rust blight, verticillium wilt, root rot, and other diseases effects.    DETAILED DESCRIPTION - A biological compound fertilizer comprises 30-55 pts. wt. chicken manure, 25-35 pts. wt. rice bran, 34-46 pts. wt. wheat bran, 10-24 pts. wt. potato, 5-9 pts. wt. sugar, 9-15 pts. wt. agar, 3-8 pts. wt. phosphate rock, 4-7 pts. wt. calcium dihydrogen phosphate, 4-7 pts. wt. calcium dihydrogen phosphate, 1-3 pts. wt. phosphate, 5-9 pts. wt. potassium dihydrogen phosphate, 4-7 pts. wt. dipotassium hydrogen phosphate, 8-12 pts. wt. Verticillium powder, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 0.1-0.2 pts. wt. Aschersonia powder, 0.3-0.5 pts. wt. caterpillar fungus powder, 1-3 pts. wt. cortex fraxini, and 1-2 pts. wt. radix stemonae.
NOVELTY - A multi-effect biological enzyme fertilizer comprises 25-35 pts. wt. potato straw, 25-35 pts. wt. highland barley straw, 25-35 pts. wt. broad bean straw, 25-35 pts. wt. wheat straw, 1-2 pts. wt. radix sophorae flavescentis, 1-2 pts. wt. pine needle, 1-2 pts. wt. Isatis root, 0.1-0.2 pts. wt. peptide powder, 0.5-0.9 pts. wt. nitrogen-phosphorus-potassium element, 0.1-0.2 pts. wt. aphid killing element powder, 0.1-0.2 pts. wt. penicillin powder, 35-45 pts. wt. chicken manure, 20-35 pts. wt. industrial waste, 14-25 pts. wt. rice hull powder, and 1-3 pts. wt. fermentation enzyme.    USE - Multi-effect biological enzyme fertilizer.    ADVANTAGE - The fertilizer can improve soil fertility and promote heavy metal decomposition in the soil.
NOVELTY - A biological compound fertilizer comprises bacteria powder, Bacillus cereus powder, Bacillus thuringiensis powder, potassium mineral powder, stone powder, grass powder, diammonium phosphate, ammonium dihydrogen phosphate, silicate containing bacteria, Bacillus subtilis, Bacillus stearothermophilus, chicken manure, Bacillus anthracis, rice bran, and wheat bran.    USE - A biological compound fertilizer.    ADVANTAGE - The fertilizer is cheap and environment-friendly, improves soil quality, can prevent soil-borne disease, does not leave residue, and has simple preparation method.    DETAILED DESCRIPTION - A biological compound fertilizer comprises 0.1-0.2 pts. wt. bacteria powder, 0.1-0.2 pts. wt. B. cereus powder, 0.1-0.2 pts. wt. B. thuringiensis powder, 4-8 pts. wt. potassium mineral powder, 5-9 pts. wt. stone powder, 6-12 pts. wt. grass powder, 4-6 pts. wt. diammonium phosphate, 3-7 pts. wt. ammonium dihydrogen phosphate, 0.01-0.02 pts. wt. silicate containing bacteria, 0.01-0.02 pts. wt. B. subtilis, 0.01-0.02 pts. wt. B. stearothermophilus, 0.01-0.02 pts. wt. chicken manure, 25-30 pts. wt. B. anthracis, 14-25 pts. wt. rice bran, and 10-16 pts. wt. wheat bran.
NOVELTY - An environment-friendly agricultural microorganism fertilizer comprises 4-9 pts. wt. rock phosphate, 8-12 pts. wt. potassium mineral powder, 15-25 pts. wt. stone powder, 24-35 pts. wt. grass powder, 14-23 pts. wt. phosphoric acid, 1-6 pts. wt. potassium chloride, 0.01-0.02 pts. wt. zinc powder, 0.01-0.02 pts. wt. Candida powder, 0.01-0.02 pts. wt. Azotobacter, 0.01-0.02 pts. wt. phosphorus containing bacteria, 0.01-0.02 pts. wt. potassium containing bacteria, 45-50 pts. wt. chicken manure, 25-35 pts. wt. rice hull powder, 45-60 pts. wt. straw, and 10-15 pts. wt. urea.    USE - An environment-friendly agricultural microorganism fertilizer.    ADVANTAGE - The fertilizer improves soil quality, and has simple preparation method, high viable bacteria content and high yield.
NOVELTY - Oxiracetam is synthesized by mixing ketene, methylene dichloride and bromine at 20-30 degrees C, decompressing, distilling, reacting with 1-4C alkyl at 20-30 degrees C for 30-50 minutes, decompressing, evaporating solvent, mixing with methanol, adding reducing agent, reacting at 15-20 degrees C, adjusting pH value to 5.5-6.5 for 0.5 hour, extracting with organic solvent, taking organic layer, evaporating, adding inorganic alkali, glycinamide hydrochloride and ethanol, heating, refluxing for 22-24 hours, concentrating, filtering and decolorizing with activated carbon.    USE - Method for synthesizing oxiracetam (claimed).    ADVANTAGE - The method is simple, safe, low-cost and environment-friendly.
NOVELTY - A manidipine hydrochloride intermediate 2-(4-benzene methyl piperazine) ethyl acetoacetate is prepared by adding base as catalyst in organic solvent, using 1-diphenyl-4-(2-hydroxyethyl) piperazine as raw material, performing transesterification of ethyl acetoacetate, concentrating, extracting salt until mixture is salt-free, and purifying.    USE - Preparation of manidipine hydrochloride intermediate 2-(4-benzene methyl piperazine) ethyl acetoacetate (claimed).    ADVANTAGE - Preparation process does not use tear gas, toxic and low flash point substance, and explosive diketene and has mild reaction process and high safety and yield, cost is reduced, and production period is shortened.
NOVELTY - This utility model claims a kind of organic matter fertilizer preparing machine, comprising an insulating heat insulating bucket cover, a stainless steel inner barrel and a shell, a stainless steel inner barrel lower part is provided with a water bath constant temperature water tank, a constant temperature water tank is provided with ventilating fan and a speed reducing motor, a stainless steel side part is provided with a stirring wheel, the stirring chain wheel as the driven chain wheel through the belt is connected to the driving chain wheel of the speed reducing motor. The stainless steel inner barrel is provided with a stirring frame, wherein the stirring structure comprises a hexagonal main shaft and fixing multiple bend knife-type stirring blade is hexagonal main axis; By using this utility model the organic material preparing machine, which can better overcome the device technology and is provided with a low cost, the operation is simple, the assembling and convenient maintenance, a method and the fertilizer efficiency, improve the working environment, reduce the consumption, green environmental protection and so on.
NOVELTY - The electrolytic gas generating module has a water container (50) provided with low water level sensor (582) that generates a low level water signal upon detecting a predetermined low level of electrolytic aqueous solution in the container. A water pump is disposed in the water storage tank (12) to deliver the solution from the tank to the container upon receiving the signal. A pressure regulator has an inlet end connected to the second gas outlet (54) of a first gas pipe (53) to regulate discharging pressure of the flow of a hydrogen and oxygen mixture at the inlet end.    USE - Electrolytic gas generating module for converting water into mixture of hydrogen and oxygen.    ADVANTAGE - The provision of a water level sensor unit, a refrigerant level sensor unit, a water pump, and a refrigerant pump eliminates unstable operation of the electrolytic gas generating module due to variation in the level of aqueous solution in the water container and variation in the level of refrigerant in the cooling tank. Prevents interruptions in the operation of the module, since the electrolytic aqueous solution in the water container and the refrigerant in the cooling tank can be automatically compensated.    DETAILED DESCRIPTION - A cooling tank (60) is connected with the outlet end of the pressure regulator to receive and cool the hydrogen and oxygen mixture from the water container (50). A second gas pipe (64) has a gas outlet (65) adjacent to the top open end for discharging the mixture from the cooling tank to the atmosphere. A safety cap (66) closes the top open end of the second gas pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows the partly exploded perspective view illustrating the installation of tubular cooling devices of the electrolytic gas generating module.    Water container (50)    First gas pipe (53)    Second gas outlet (54)    Cooling tank (60)    Second gas pipe (64)    Gas outlet (65)    Safety cap (66)    Low water level sensor (582)
NOVELTY - This invention relates to production of hydrogen-bearing gas and can be used in processing of Fischer-Tropsh process waste products in the presence of porous membrane-catalytic system. Porous catalytic membrane is produced by vibratory compaction of fine mix containing nickel and cobalt at 1:1 ratio and treated in muffle furnace at spontaneous ignition temperature, then cured and cooled. Invention covers also the process of processing Fischer-Tropsh process waste products. Proposed method comprises processing methane, carbonic acid and organic substances diluted in water (methanol, ethanol, methyl ethyl ketone, acetic acid and acetone) by carbonic acid-steam conversion in the presence of said catalytic module at 680-780 degrees C, 1-1.5 atm and the rate of feeding the initial steam-gas mix along with water steam released in the process, 16000-96000 p-1 to obtain conversion products, that is synthesis gas and water cleaned of organic substance impurities.    USE - Process engineering.    ADVANTAGE - Efficient process, higher yield of valuable hydrocarbons.4 cl, 1 dwg, 4 tbl, 9 ex
NOVELTY - A biomass processing system comprises 1st unit (11) containing hydrolysis tank which hydrolyzes biomass, 2nd unit (12) containing fermenter which is connected to hydrolysis tank of 1st unit and ferments hydrolyzed biomass and desulfurizing apparatus which desulfurizes gas emitted by fermenter, and 3rd unit (13) containing gas decomposition apparatus (131) which decomposes gas supplied through desulfurizing apparatus of 2nd unit. Arrangement of 1st unit and 2nd unit is according to treatment process of biomass.    USE - A biomass processing system (claimed).    ADVANTAGE - The biomass processing system has a simple structure.    DETAILED DESCRIPTION - A biomass processing system comprises 1st unit (11) containing hydrolysis tank which hydrolyzes biomass, 2nd unit (12) containing fermenter which is connected to hydrolysis tank of 1st unit and ferments hydrolyzed biomass and desulfurizing apparatus which desulfurizes gas emitted by fermenter, and 3rd unit (13) containing gas decomposition apparatus (131) which decomposes gas supplied through desulfurizing apparatus of 2nd unit. Arrangement of 1st unit and 2nd unit is according to treatment process of biomass. The 3rd unit is independent of 1st unit and 2nd unit. The system produces gas containing methane by methane-fermenting biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows an external view of the biomass processing system. (Drawing includes non-English language text).    1st unit (11)    2nd unit (12)    3rd unit (13)    Crushing apparatus (100)    Gas decomposition apparatus (131)
NOVELTY - A vehicular hydrogen-oxygen electrolyzing device comprises main body (1), sealing pairs (2), electrolysis unit bracket (3), separating sheet (4), and discharge port (21).    USE - Vehicular hydrogen-oxygen electrolyzing device.    ADVANTAGE - The device has high heat energy, and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of vehicular hydrogen-oxygen electrolyzing device.    Main body (1)    Sealing pairs (2)    Electrolysis unit bracket (3)    Separating sheet (4)    Discharge port (21)
NOVELTY - Rutin is separated and purified by crushing flos sophorae immaturus, soaking in limewater, extracting ultrasonically, filtering, repeating, and combining; adding hydrochloric acid, precipitating, filtering, washing with water, and drying; mixing ethylene oxide-propylene oxide copolymer and water, adding salt, mixing, adding extract, mixing, centrifuging, and separating; warming in water bath at 50-70 degrees C for 10-30 minutes, centrifuging at speed of 1000-2000 revolutions/minute for 3-5 minutes, and separating; and cooling, standing overnight, precipitating, and filtering.    USE - Method for separating and purifying rutin (claimed).    ADVANTAGE - The method is economical, environment-friendly, energy-saving, and yields rutin of high purity.    DETAILED DESCRIPTION - Rutin is separated and purified by:    (A) crushing flos sophorae immaturus, soaking in saturated limewater for 30-40 minutes, extracting ultrasonically at frequency of 20 kHz for 20-60 minutes, filtering, repeating, and combining;    (B) adding hydrochloric acid to pH value of 3-4, precipitating, filtering, washing with water for 3 times, and drying at less than or equal to 60 degrees C;    (C) mixing ethylene oxide-propylene oxide copolymer and water with volume ratio of 1-3:1-4, adding salt, mixing, adding 2.0-5.0 mg/mL extract, mixing, centrifuging with speed of 1000-2000 revolutions/minute for 2-5 minutes, and separating;    (D) warming in water bath at 50-70 degrees C for 10-30 minutes, centrifuging at speed of 1000-2000 revolutions/minute for 3-5 minutes, and separating; and    (E) cooling, standing overnight, precipitating, and filtering.
NOVELTY - The method involves injecting waste oil raw material into a pyrolysis pipeline. A hot steam of the pyrolysis pipeline is processed at temperature of 60-62 degrees Celsius. Temperature of a heating environment is controlled at 180-220 degrees Celsius. A catalyst bed layer of a molecular sieve is formed on the pyrolysis pipeline. The pyrolysis pipeline is synthesized and dehydrated to obtain carbon biological liquid fuel oil.    USE - Waste oil catalytic process based methyl alcohol fuel producing method.    ADVANTAGE - The method enables providing the biological waste oil by steam thermal evaporation to obtain petrol and diesel oil in an easy manner, improving product quality and dynamic property of biological liquid fuel methanol diesel oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a waste oil catalytic process based methyl alcohol fuel production device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a waste oil catalytic process based methyl alcohol fuel production device.
NOVELTY - A manganese oxide and hydrogen co-producing method involves subjecting electrolytic manganese metal sheet and water to hydrogen evolution reaction in a sealed reactor and collecting hydrogen and manganese hydroxide generated during reaction. The collected manganese hydroxide is subjected to oxidation reaction to obtain manganese tetroxide.    USE - Method for co-producing manganese tetroxide and hydrogen.    ADVANTAGE - The method enables co-producing manganese tetroxide and hydrogen in a simple, convenient, economical and safe manner.
NOVELTY - Synchronization of methanol biodiesel oil and glycerol carbonate comprises adding natural oil, dimethyl carbonate and methanol at mass ratio of 1:(1-5):(1-10) into reaction kettle, adding 5-20% alkali, stirring and heating at 60-90 degrees C for 4-8 hours, cooling to room temperature, filtering, washing, evaporating filtrate to obtain light yellow liquid which is the biodiesel oil crude product, extracting with equal volume of methanol for 2-3 times and removing methanol to obtain glycerol carbonate. The natural oil is mixture of acid, dehydrated vegetable oils and animal oils.    USE - Method for synchronizing methanol biodiesel oil and glycerol carbonate (claimed).    ADVANTAGE - The method reduces processing cost.    DETAILED DESCRIPTION - Synchronization of methanol biodiesel oil and glycerol carbonate comprises adding natural oil, dimethyl carbonate and methanol at mass ratio of 1:(1-5):(1-10) into reaction kettle, adding 5-20% alkali, stirring and heating at 60-90 degrees C for 4-8 hours, cooling to room temperature, filtering, washing, evaporating filtrate to obtain light yellow liquid which is the biodiesel oil crude product, extracting with equal volume of methanol for 2-3 times and removing methanol to obtain glycerol carbonate. The natural oil is mixture of acid, dehydrated vegetable oils and animal oils. The alkali is sodium carbonate, sodium hydroxide, potassium hydroxide and/or barium hydroxide.
NOVELTY - A photovoltaic and photothermal combined system comprises light focusing device (1), heat collecting pipe (2), light splitting device (3), integrated device (4), electrolytic groove (11), photovoltaic component (13), heat-insulating material (17), first heat-exchange tube (15), second heat-exchange tube (21), first water tank (5), second water tank (7), electrolytic cell (19) and electrolytic water pipeline (12).    USE - Photovoltaic and photothermal combined system used for production of hydrogen from ammonia.    ADVANTAGE - The system improves utilization efficiency of solar energy by more than 60%, improves efficiency of electrolytic hydrogen production by 10-15%, improves overall efficiency by 20%, and reduces temperature of photovoltaic component.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of photovoltaic and photothermal combined system.    Light focusing device (1)    Heat collecting pipe (2)    Light splitting device (3)    Integrated device (4)    First water tank (5)    Second water tank (7)    Electrolytic groove (11)    Electrolytic water pipeline (12)    Second heat-exchange tube (21)
NOVELTY - The tank has spherical octagon stainless steel lid (2) which is welded onto the tank. The lid is connected to cathode shaft and anode shaft for supplying negative charge current and positive charge current to cell plate set (11). The top and the bottom cell plates are positioned, so that holes on the inner circle of plates are arranged opposite to one another. The permanent magnets (12) are covered in stainless steel cases, and are positioned in between the cell plates. The electromagnetic field is generated, when direct current is passed through the electrolyte solution.    USE - WDHI hydrogen separation tank.    ADVANTAGE - The pure hydrogen can be provided to use in the combustion engine with other fuel such as petrol, LPG, and CNG, so that fuel cost and the amount of carbon monoxide emission can be reduced. The permanent magnets are completely covered in stainless steel case, so that corrosion of permanent magnet can be prevented and the service life of the magnets can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen separation tank.    Stainless steel lid (2)    Shaft (5)    Octagon cell plate (11)    Permanent magnet (12)
NOVELTY - The oval cylinder-shaped hydrogen production tank has a tank with a bottom which is sealed with a stainless steel plate. A stainless steel pipe is connected to the bottom of the side of the tank. The top of the stainless steel pipe contains a braid for connecting an electrolyte solution meter. An electrolyte solution refilling pipe has a bottom connected to the top edge of the tank and to the electrolyte solution meter pipe. The top of the electrolyte solution refilling pipe is 9 centimeters taller than an oval stainless steel lid (10) and contains its own lid.    USE - Oval cylinder-shaped hydrogen production tank used for production of hydrogen gas.    ADVANTAGE - Reduces carbon dioxide and carbon oxide emission from fossil fuel combustion to help yield global warming crisis. Allow electrolyte solution to flow through and constantly create difference in voltage since holes are formed on cell plates.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a cell plate;    (2) a permanent magnet; and    (3) a neutral shaft.    DESCRIPTION OF DRAWING(S) - The drawing shows the side view of the arrangement of cell plates and magnets connected to shafts.    Anode shaft (3)    Neutral shaft (4)    Cathode shaft (5)    Lid (10)    Hydrogen gas pipe (11)
NOVELTY - The tank has semi-spherical stainless steel lid (2) which is welded onto the tank. A stainless wire is extended into the tank. The electrolyte solution level meter pipe measures the electrolyte solution level. The top of the lid contains holes for installing anode shaft, cathode shaft, thermometer and hydrogen pipe connector (7). A cathode supplies negative electrical current from direct current (DC) power supply to lid, while anode supplies positive electrical current from DC power supply to anode shaft. The center holes are formed on the cell plates.    USE - Hydrogen separation tank.    ADVANTAGE - The permanent magnets are completely covered in stainless steel case, so that corrosion of permanent magnet can be prevented and the service life of the magnets can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen separation tank.    Cylinder tank (1)    Stainless steel lid (2)    Hydrogen pipe connector (7)    Shaft (8)    Round cell plate (11)
NOVELTY - The tank has a cooling tank portion that is large enough to hold hydrogen separation tank inside. The top of tank portion is provided with a lid with cooling liquid refill pipe (2), cooling liquid checking pipe (3), pressure release valve (4) and electrolyte solution level meter (17). The tank portion is designed to hold cooling liquid. A stainless steel bottom plate is welded tightly to tank portion and to prevent cooling liquid leakage. The holders are attached to the bottom of the cooling tank portion and are configured to hold the tank portion tightly to a structure.    USE - Stainless steel HPC2 liquid cooling system tank for car radiator (claimed).    ADVANTAGE - The stainless steel bottom plate is arranged to prevent cooling liquid leakage, and the holders are attached to the bottom of the cooling tank portion and are configured to hold the tank portion tightly to a structure, so that the heat and the toxic gas produced by fossil fuel usage can be reduced and the direct current in the electrolysis process can be stabilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for HPC2 hydrogen separation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of cell plates and permanent magnet connected to anode shaft.    Cooling liquid refill pipe (2)    Cooling liquid checking pipe (3)    Pressure release valve (4)    Electrolyte solution level meter (17)    Permanent magnet (20)
NOVELTY - Processing lignocellulosic biomass comprises: providing soft lignocellulosic biomass feedstock; pretreating the feedstock at pH of 3.5-9 in a single stage pressurized hydrothermal pretreatment to very low severity; separating the pretreated biomass into an solid fraction and a liquid fraction; hydrolyzing the solid fraction with or without addition of supplemental water content using enzymatic hydrolysis catalyzed by an enzyme mixture; and subsequently mixing the separated liquid fraction and the hydrolyzed solid fraction.    USE - The method is useful for processing lignocellulosic biomass including wheat straw, corn stover, sugar cane bagasse, sweet sorghum bagasse, empty fruit bunches (all claimed), corn cobs, rice straw, oat straw, barley straw, canola straw, rye straw, sorghum, soybean stover, switch grass, bermuda grass and other grasses, beet pulp and/or corn fiber.    ADVANTAGE - The method economically processes lignocellulosic biomass with improved profitability and water holding capacity.    DETAILED DESCRIPTION - Processing lignocellulosic biomass comprises: providing soft lignocellulosic biomass feedstock; pretreating the feedstock at pH of 3.5-9 in a single stage pressurized hydrothermal pretreatment to very low severity such that the pretreated biomass is characterized by having a xylan number of 10% or higher; separating the pretreated biomass into an solid fraction and a liquid fraction; hydrolyzing the solid fraction with or without addition of supplemental water content using enzymatic hydrolysis catalyzed by an enzyme mixture comprising endoglucanase, exoglucanase, beta -glucosidase, endo-xylanase, xylosidase and acetyl xylan esterase activities; and subsequently mixing the separated liquid fraction and the hydrolyzed solid fraction, where xylo-oligomers in the liquid fraction are degraded to xylose monomers by the action of enzyme activities remaining within the hydrolyzed solid fraction.
NOVELTY - Producing hydrogen involves steam reforming a hydrocarbon feed in the presence of a steam reforming catalyst, where the catalyst comprises a precious metal contained on a ceria-zirconia-praseodymium oxide support.    USE - For producing hydrogen (claimed) used for fuel cells for converting chemical energy to electric energy through electrochemical reaction of hydrogen and oxygen.    ADVANTAGE - The new catalyst has lower tendency for coke accumulation (more coke tolerant) and allows the steam reformer to operate at lower reaction temperatures and steam concentrations, which increases the efficiency of the fuel cell system, providing large-scale successful commercialization of fuel cell systems. The catalyst yields a reduced amount of coke and consequently has improved retention of activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the new catalyst for steam reforming a hydrocarbon feed to hydrogen comprising rhodium contained on a support CexZryPrzO2, where rhodium is present in 0.1-10 wt.% based on support.    z=0.1-0.5;    x/y=1-19;    x+y+z=1.    .
NOVELTY - A waste water treatment system comprises a tank (10) to receive and hold waste water, inlet unit and an unit to remove treated waste water and an unit to remove gases released from the waste water as a result of anaerobic digestion of waste water and an unit to retain and remove sludge; unit to distribute waste water uniformly at bottom of the tank; an unit to direct supply all released gas to at least one gas collection chamber (12) in the tank; and an unit to collect treated waste water for release into acceptable waterways.    USE - As waste water treatment system (claimed).    ADVANTAGE - The waste water treatment system does not utilize electrical energy for operation, thus saving in electrical energy; and collects the gases released by the anaerobic digestion for subsequent disposal in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating waste water by anaerobic method involving introducing waste water from the top of the tank uniformly to feed points at the bottom of the tank; allowing anaerobic digestion of the waste water; directing released gases to flow upward to a gas collection chamber at surface level of water in the tank; collecting released gases in at least one gas collection chamber; and disposing of supernatant liquid and disposing of sludge.    DESCRIPTION OF DRAWING(S) - The figure shows partial cross-sectional view of a tank.    Tank (10)    Gas collection chamber (12)    Overflow channel (14)    Support beam (20)    Separator sheet (22)
NOVELTY - Substituted metal complex (I) is new.    USE - (I) is useful as a catalyst, which is useful for generating hydrogen and/or oxygen gases, for generating methanol, hydrocarbons and/or oxygen gases, and in a photo-electrochemical cell (all claimed) for electrolysis of water molecules.    ADVANTAGE - (I) efficiently electrolyzes the water or reduces carbon dioxide to obtain affordable and sustainable alternative source of energy.    DETAILED DESCRIPTION - Substituted metal complex of formula (I) is new.    M = Ru or Os;    L = bidentate ligand;    L2 = tridentate ligand;    L3 = monodentate ligand; and    n = 1 or 2.    INDEPENDENT CLAIMS are included for:    (1) a catalyst comprising (I);    (2) a method of generating hydrogen and/or oxygen gases, comprising providing the catalyst comprising (I) and adding the catalyst to an electrolytic media under a condition effective to generate hydrogen and/or oxygen; and    (3) a method of generating methanol, hydrocarbons and/or oxygen gases comprising providing the catalyst and a supporting substrate, and adding the catalyst to a electrolytic media under a condition effective to generate methanol, hydrocarbons and/or oxygen.
NOVELTY - Filter element comprises: a filtration media (23); and an ion exchange media (29).    USE - The filter element is useful in filtration system for removing undesirable soap from diesel fuel (claimed), ultra-low sulfur diesel, hydrotreated distillate fuel, or biodiesel.    ADVANTAGE - The filter element utilizes: the filter media that has mean flow pore size of less than 5 mu , and beta ratio of greater than 20 at 4 mu m(c) (all claimed) thus exhibiting greater than 99% removal efficiency; ion exchange media resin that is easier to handle, process and package; and the resin that has the potential to only be active when the soap contaminant is present, remains dormant (if no soap is present) and has extended service life.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a filtration system (10) for filtering a fluid, comprising: ion exchange media that is configured to remove at least one dissolved metal ion from the fluid; a filter media that is configured to remove soap that is present in the fluid; and at least one housing (18) that contain the ion exchange media and the filter media;    (2) removing undesirable soap in fuel, comprising: removing soluble soap contained in the fuel by ion exchange; and removing insoluble soap contained in the fuel by filtration; and    (3) a system for controlling an amount of soluble and insoluble soap in an application fluid, comprising: a means for reducing at least one dissolved metal ion from the application fluid; and a means for reducing soap from the application fluid.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic view of the filtration system where the ion exchange media and the filter media reside in different housings.    Filtration system (10)    Housings (18)    Filter media (23)    Ion exchange media (29)
NOVELTY - Hydrogen generation cell (100) which releases an amount of hydrogen proportional to amount of current flowing through the cell, during the flow of electric current, comprises an electrochemically oxidizable anode (120), a hydrogen cathode (140) which forms a pouch (170) defining a cavity optionally during excess pressure of hydrogen, an electrolyte, and a housing (110) surrounding the anode, cathode and the electrolyte.    USE - Used as a hydrogen generation cell.    ADVANTAGE - The hydrogen generation cell exhibit reduced risk of occurrence of leakage compared to conventional cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of the hydrogen generation cell.    Hydrogen generation cell (100)    Housing (110)    Electrochemically oxidizable anode (120)    Hydrogen cathode (140)    Pouch (170)
NOVELTY - The apparatus (1) has a liquid process unit (2) with which a carrier (3) which carries the microorganisms which decomposes a to-be-processed substance contained in a to-be-processed liquid (10) is filled. The to-be-processed liquid is distributed to the liquid process unit, and the to-be-processed substance is decomposed. The carrier is provided with the material containing the substance used as the nutrient of the microorganisms.    USE - Apparatus for processing liquid such as organic waste water, domestic waste water, industrial wastewater, sewage, underground water, fishery water and seawater, for use in fish breeding facility.    ADVANTAGE - The microorganisms are proliferated by making into nutrient the to-be-processed substance contained in the nutrient of the microorganisms included in the carrier and the to-be-processed liquid. Hence the liquid can be processed efficiently at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a liquid processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the liquid processing apparatus.    Liquid processing apparatus (1)    Liquid process unit (2)    Carrier (3)    To-be-processed liquid (10)    Oxidation-reduction potential measurement unit (15)
NOVELTY - Mixed waste containing plastic waste and organic waste is ground by crushing (2), resulted product is dried (3), and classified (4) into plastic dry ground material and organic dry ground material. The obtained plastic dry ground material and organic dry ground material are mixed (5), to obtain mixed raw material. The mixed raw material is subjected to molding by solid-fuel manufacturing process (6), to obtain solid fuel.    USE - Processing of mixed waste containing plastic waste and organic waste for separating mixed waste discharged from convenience store and food-processing factory used, and for manufacturing solid fuel (all claimed) used as energy source.    ADVANTAGE - The mixed waste containing plastic waste and organic waste is processed by efficient, reliable, economical and environmentally-friendly method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) processing apparatus, which consists of pulverization device, drying apparatus, sorting apparatus, mixing preparation apparatus, and processing apparatus comprising solid-fuel manufacturing apparatus;    (2) manufacture of solid fuel; and    (3) separation of mixed waste containing plastic waste and organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view explaining processing of mixed waste. (Drawing includes non-English language text)    Processing system (1)    Crushing process (2)    Drying process (3)    Classification process (4)    Mixing preparation process (5)    Solid-fuel manufacturing process (6)
NOVELTY - Method for preparing ethanol from lignocellulosic raw material, involves performing saccharification and fermentation simultaneously by continuously supplying the raw material containing lignocellulosic raw material into the supply port of the culture tank, continuously discharging the stock suspension from the discharge port, discharging the stock suspension from the discharge port, passing through ion exchange resin, circulating the supply to the culture tank, and maintaining the acetic acid concentration in raw material suspension discharged.    USE - The method is useful for preparing the ethanol (claimed).    ADVANTAGE - The method improves the productivity of ethanol by removing the acetic acid generated efficiently.    DETAILED DESCRIPTION - Method for preparing ethanol from lignocellulosic raw material, involves performing saccharification and fermentation simultaneously by continuously supplying the raw material containing lignocellulosic raw material into the supply port of the culture tank, continuously discharging the stock suspension from the discharge port of the culture tank, discharging the stock suspension from the discharge port of the culture tank, where intake disposed at a position different from the discharge port, passing through ion exchange resin, circulating the supply to the culture tank, and maintaining the acetic acid concentration contained in raw material suspension discharged from the discharge port of the culture tank to be 1 %mass or less.
NOVELTY - Producing racemic 3-(carbamoylmethyl)-5-methylhex-anoic acid (I), comprises (a) heating the (S)-isomer of (I) in the presence of a metal salt in an organic solvent at a temperature of 80-140 degrees C, where the (S)-isomer is substantially free of the (R)-isomer or a mixture of the (R)- and the (S)-isomer of (I) and (S)-isomer is present in predominant amount, and (b) isolating the (I) from the reaction mixture obtained in the step (a).    USE - The process is useful for producing (I) (claimed), which is useful as intermediate for preparing pregabalin used as antivasculant drug for neuropathic pain.    ADVANTAGE - The improved method produces (I) with good yield and purity and without use of an organic base such as piperidine and number of reaction steps in an cost-effective, time-effective and environment friendly manner.
NOVELTY - A thermoplastic resin composition comprises biomass-derived resin.    USE - Thermoplastic resin composition is used for automobile upholstery material molded product (claimed).    ADVANTAGE - The automobile upholstery material obtained using thermoplastic resin composition replaces petroleum-based thermoplastic resin and reduces generation of carbon dioxide, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for automobile upholstery material molded product, which has sheet manufactured using thermoplastic resin composition.
NOVELTY - Method for hydrolyzing pretreated cellulosic material involves subjecting the pretreated cellulosic material to (a) a cellulolytic enzyme composition, (b) a polypeptide having cellulolytic enhancing activity, (c) a peroxidase and (d) a nonionic surfactant and/or a cationic surfactant under suitable conditions.    USE - The method is useful for hydrolyzing pretreated cellulosic material using the composition used for producing fermentation product, preferably ethanol (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing fermentation product involves (a) hydrolyzing pretreated cellulosic material, (b) fermenting the hydrolyzed material with one or more fermenting microorganisms, and (c) optionally recovering the fermentation product from the fermentation; and    (2) composition comprising a polypeptide having cellulolytic enhancing activity, peroxidase, nonionic surfactant and cationic surfactant.
NOVELTY - Removing one or more components from a butanol based composition comprising one or more components, involves processing the butanol based composition such that at least one component is substantially removed.    USE - The method is useful for removing one or more components from a butanol based composition comprising one or more components (claimed).    ADVANTAGE - The method results in a composition comprising bio-produced butanol having reduced level of certain deleterious bio-produced components.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a composition comprising bio-produced isobutanol and bio-produced isobutyric acid, where the amount of bio-produced isobutyric acid is up to 0.5 wt.% of the composition; and    (2) a fuel composition comprising bio-produced isobutanol, comprising: (a) the composition, and (b) a hydrocarbon-containing fuel.
NOVELTY - Manufacture of solid fuel involves mixing pig ordure precipitate, acetic acid and sodium hypochlorite, maintaining moisture content, dehydrating to obtain dehydrated pig ordure, maintaining moisture content of peat, mixing the peat and the pig ordure, sterilizing obtained mixture by mixing pig ordure mixture, acetic acid and sodium hypochlorite, dehydrating, performing pellet-forming process on obtained mixture into constant shape and size, and drying obtained pellets using microwave drier, such that moisture content becomes 6-8% to obtain solid fuel.    USE - Manufacture of solid fuel (claimed).    ADVANTAGE - The method provides highly-efficient solid fuel.    DETAILED DESCRIPTION - Manufacture of solid fuel involves sterilizing bad smell generated in pig ordure precipitate by mixing 98-99 wt.% pig ordure precipitate, 0.15-0.25 wt.% acetic acid and 0.35-0.75 wt.% sodium hypochlorite and maintaining moisture content of 65-75% in reservoir, performing dehydration process on obtained pig ordure precipitate, such that pig ordure solid material maintains moisture of 45-50% through dehydration apparatus including belt press apparatus to obtain dehydrated pig ordure having solid content of 45-50%, maintaining moisture content in the pig ordure solid as 70-80%, maintaining moisture content of peat as 20-30 wt.%, mixing the peat and the pig ordure, sterilizing obtained mixture by mixing 99-99.5% pig ordure mixture, 0.15-0.25 wt.% acetic acid and 0.35-0.75 wt.% sodium hypochlorite, dehydrating, such that moisture content in the mixture is 20-25%, performing pellet-forming process on obtained mixture into constant shape and size, and drying obtained pellets using microwave drier, such that moisture content becomes 6-8%, to obtain solid fuel. An INDEPENDENT CLAIM is included for solid fuel.
NOVELTY - Mixing fermentation substrate (6) in a fermenter (2) of a biogas plant, comprises uniformly distributing a substrate stream which is pumped into a gas chamber (8) of the fermenter, on surface (7) of the fermentation substrate, during substrate circulation. The speed at which the substrate stream is pumped into the gas chamber is varied.    USE - The method is useful for mixing fermentation substrate in a fermenter of a biogas plant.    ADVANTAGE - The method ensures uniform distribution of the substrate stream on larger surfaces.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above method, comprising a recirculation pipe and a circulating pump which is associated with a pump speed controller.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method for mixing the fermentation substrate in the fermenter of the biogas plant.    Biogas reactor (1)    Fermenter (2)    Fermentation substrate (6)    Fermentation substrate surface (7)    Gas chamber (8)
NOVELTY - Biogas plant comprises a fermenter tank (1), an aggregate carrier (2), which is mounted in a vertically aligned manner in the fermenter tank, and a aggregate (10), preferably a submersible motorized stirring device, which is mounted height adjustably at the aggregate carrier using a height adjustment device (11). The height adjustment device has a traction chain, which is guided over at least one rotatably mounted drive wheel (15) and is connected to the aggregate so that the aggregate is pulled upwards during rotational operation of the drive wheel in a first direction.    USE - Used as the biogas plant.    ADVANTAGE - The biogas plant adjusts the aggregate along the aggregate carrier in the fermenter tank in a simple manner over a prolonged period.    DETAILED DESCRIPTION - Biogas plant comprises a fermenter tank (1), an aggregate carrier (2), which is mounted in a vertically aligned manner in the fermenter tank, and a aggregate (10), preferably a submersible motorized stirring device, which is mounted height adjustably at the aggregate carrier using a height adjustment device (11). The height adjustment device has a traction chain, which is guided over at least one rotatably mounted drive wheel (15) and is connected to the aggregate so that the aggregate is pulled upwards during rotational operation of the drive wheel in a first direction and the is lowered is lowered during rotational operation of the drive wheel in a second, opposite direction.    DESCRIPTION OF DRAWING(S) - The figure shows a partial schematic view of the fermenter tank of the biogas plant.    Fermenter tank (1)    Aggregate carrier (2)    Aggregate (10)    Height adjustment device (11)    Drive wheel (15)
NOVELTY - Fertilizer composition comprises: 12-17 wt.% of a limestone product; 4-8 wt.% of an iron product; up to 4 wt.% of a manganese product; up to 5 wt.% of a sulfate of potash-magnesia, humus extract product; 20-25 wt.% of a sulfate of potash product; and 50-54 wt.% of a humic acid dispersing product.    USE - The fertilizer composition is useful for providing nutrients to turf and other plants, preferably to warm and cool season turf plants. Tests details are described but no results given.    ADVANTAGE - The fertilizer composition: is environmentally efficient and effective, and can be utilized year round without restriction for warm and cool season turf needs; increases water retention, aids in micronutrient uptake and provides soil biology; acts as a soil conditioner, thus reducing the amount of irrigation time needed for the turf to which the fertilizer is applied, thus saving water; is staining free; and does not contribute to red/blue algae blooms, as conventional fertilizers do.
NOVELTY - Improved process for preparing roflumilast comprises: oxidizing 3-(cyclopropylmethoxy)-4-(difluoromethoxy)benzaldehyde with Jones reagent in a solvent to obtain 3-(cyclopropyl-methoxy)-4-(difluoromethoxy)benzoic acid; converting 3-(cyclopropylmethoxy)-4-(difluoromethoxy) benzoic acid to acid chloride by treating with reagent; reacting acid chloride with 3,5-dichloropyridin-4-amine in presence of base in a solvent to obtain roflumilast; and optionally, recrystallizing the roflumilast from solvent.    USE - The process is useful for preparing roflumilast (claimed), where the roflumilast is useful for reducing risk of chronic obstructive pulmonary disease (COPD) exacerbations in patients with severe COPD associated with chronic bronchitis and a history of exacerbations. No biological data given.    ADVANTAGE - The process is capable of economically preparing roflumilast with high purity of greater than 99.9 wt.% in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an improved process for preparing 3-(cyclopropylmethoxy)-4-(difluoromethoxy) benzoic acid, comprising oxidizing 3-(cyclopropylmethoxy)-4-(difluoromethoxy) benzaldehyde with Jones reagent to obtain 3-(cyclopropylmethoxy)-4-(difluoromethoxy) benzoic acid.
NOVELTY - An ezetimibe compound (I) is new.    USE - Ezetimibe compound is used for preparing nitrogen-containing compound for preparing hydroxyl group-containing compound (all claimed).    ADVANTAGE - The ezetimibe compound is economically prepared without polluting the environment, and synthesized into the chiral drug ezetimibe, by a simple method.    DETAILED DESCRIPTION - An ezetimibe compound of formula (I) is new.    P=H, acetyl, propionyl, tertbutyloxycarbonyl, benzyl, benzoyloxycarbonyl, triphenylmethyl, trimethylsilyl, tert-butyldimethysilyl, tert-butyldiphenylsilyl or diphenylmethysilyl;    R1=H, methyl, ethyl, isopropyl, n-butyl, t-butyl, benzyl, allyl or adamantly;    X=H or CO2R2;and    R2=H, methyl, ethyl, isopropyl, n-butyl, t-butyl, benzyl, allyl or adamantyl.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of ezetimibe compound;    (2) preparation of nitrogen-containing compound of formula (II), which involves carrying out cyclization reaction of the compound (I) in the presence of base;    (3) preparation of hydroxyl group-containing compound of formula (III), which involves carrying out cyclization reaction of fluorine-containing compound of formula (IV) in the presence of base (A), obtaining nitrogen-containing compound of formula (V), carrying out carbonyl asymmetrical reduction reaction of obtained compound in organic solvent, obtaining hydroxyl group-containing compound of formula (VI) and removing protection group from the obtained compound; and    (4) carbonyl group-containing compound, which is of formula (VII).    Z=O-LG or group of formulae (i).
NOVELTY - Dehydrating ethanol comprises removing ethylene light components including methane, carbon monoxide and hydrogen light component using a rectifying tower, isolating ethylene containing light components in the tower, and condensing liquid component to obtain liquid vinyl products at the bottom of the rectifying tower.    USE - The method is useful for dehydrating ethanol (claimed).
NOVELTY - Production of grilling charcoal comprises crushing charcoal, bamboo charcoal, or burned rice straw into particle size of less than 1 mm to obtain carbon powder; mixing caustic starch, carboxymethyl cellulose, dextrin, and water at weight ratio of 3:1:3:4 to obtain binder; and mixing binder, ethanol, and carbon powder to obtain grilling charcoal.    USE - Production of grilling charcoal.    ADVANTAGE - The method has simple steps, low cost, and short production period. It produces grilling charcoal that is safe, stable, does not generate harmful smoke or dust, and has long burning period.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for producing grilling charcoal (Drawing includes non-English language text).
NOVELTY - Preparation of solid molded fuel comprises drying pig manure to reduce moisture content to 10-25%; crushing and sieving; adding 2-5% desulfurization deodorant and anti-mildew additive; uniformly mixing to obtain dried pig manure raw materials; uniformly mixing 20-100 wt.% pig manure raw materials, 0-80% biomass, and 0-20% coal to obtain raw material mixture; and molding mixture in forming machine to obtain solid fuel.    USE - Preparation of solid molded fuel in form of particulate solid fuel or rod shaped (claimed).    ADVANTAGE - The method is simple and easy to perform, energy-saving and environment-friendly, has high processing efficiency, low manufacturing cost, and suitable for large-scale industrial production. It produces solid molded fuel that is odorless, easy to mold, easy to transport and store, has high combustion efficiency, and low secondary pollutant emissions. It achieves harmless treatment and resource utilization of manure, thus effectively solving disposal problem of excess manure.
NOVELTY - Generating biogas in a biogas plant (1), comprises fermenting biomasses as organic substrates (5) in a fermenter tank (2) of the biogas plant, by irradiating at least a part of the organic substrate by at least one irradiation device having a high-frequency energy with a high-frequency signal of 100-200 MHz, which is modulated with a low frequency signal of 1-1000 Hz, to produce biogas. The fermentation is performed in an anaerobic-, continuous single-stage wet anaerobic fermentation process.    USE - The method is useful for generating biogas in a biogas plant (claimed).    ADVANTAGE - The method achieves a high biogas yield with a very high methane content, and thus it ensures increase in the recyclable energy from biogas production, by utilizing increased methane yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of biogas plant with the fermenter tank.    Biogas plant (1)    Fermenter tank (2)    Organic substrates (5)    Bypass-tube (18)    Circulating pump (19)
NOVELTY - Biomass is continuously flash distilled by drying straw-based raw material to moisture content of approximately 12%, crushing to length of 5 cm, dehydrating with flue gas to moisture content of approximately 3%, and heating at 130-140 degrees C; distributing using blower, contacting with radiation plate, and carbonizing at 300 degrees C for 3 seconds; dedusting, cooling, settling, spray cooling with pyroligneous acid to 30-40 degrees C, heating, recycling acid, and pressurizing; and discharging anaerobically, cooling, bagging charcoal, removing tar, adding alkaline water to neutralize, and cyclone separating.    USE - Method for continuously flash distilling biomass (claimed) for producing fuel gas, charcoal and pyroligneous acid.    ADVANTAGE - Product fuel gas has heating value of 4500 kcal/m3.
NOVELTY - A butanol-gasoline blend comprises gasoline and 10-30 %mass secondary-butanol.    USE - Butanol-gasoline blend (claimed).    ADVANTAGE - The butanol-gasoline blend is economical and biodegradable and has high octane number and excellent anti-knocking property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of butanol-gasoline blend, which involves uniformly mixing gasoline and butanol at normal temperature and normal pressure and filtering.
NOVELTY - Biomass hydrothermal decomposition system, has biomass supply unit, hydrothermal decomposition unit, biomass-solid extraction unit that extracts biomass solids from the hydrothermal decomposition unit, enzymatic liquefaction tank that communicates with the biomass-solid extraction unit and, when the extracted biomass solids are added, supplies an enzyme to the biomass solids to liquefy the biomass solids, and discharge unit that discharges the liquefied biomass solids under elevated pressure to atmospheric pressure.    USE - The hydrothermal system is useful for decomposing biomass which is useful for producing sugar solution and alcohol (all claimed).    ADVANTAGE - In system, introduction amount of water at the time of carrying out slurrying process will be reduced, as unnecessary supply of slurry water from exterior is avoided.    DETAILED DESCRIPTION - Biomass hydrothermal decomposition system, has biomass supply unit that supplies biomass starting material under atmospheric pressure to elevated pressure, where the biomass starting material comprises cellulose, hemicellulose and lignin, hydrothermal decomposition unit that hydrothermally decomposes the biomass starting material using pressurized hot water to dissolve the lignin component and the hemicellulose component in the pressurized hot water, biomass-solid extraction unit that extracts biomass solids from the hydrothermal decomposition unit, enzymatic liquefaction tank that communicates with the biomass-solid extraction unit and, when the extracted biomass solids are added, supplies an enzyme to the biomass solids to liquefy the biomass solids, and discharge unit that discharges the liquefied biomass solids under elevated pressure to atmospheric pressure. INDEPENDENT CLAIMS are included for the following:    (1) sugar solution production method using the above-mentioned biomass; and    (2) alcohol preparation method.
NOVELTY - Processing apparatus for biomass, has saccharification/fermentation unit to ferment biomass in which biomass is saccharified using saccharogenic amylase fermentation microorganism, evaporator which evaporates alcohol or an organic acid from the produced mash, rectifier which rectifies evaporated liquid from evaporator, processing unit, and returning unit for returning the processed liquid to return discharged waste liquid.    USE - The apparatus is useful for processing biomass (claimed).    ADVANTAGE - The apparatus recycles the discharged waste liquid, and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of making biomass, which involves reacting fermentation microorganism with saccharogenic amylase, saccharifying the mixture, fermenting saccharified mixture, evaporating alcohol or an organic acid from fermented mash using evaporator, rectifying the evaporated liquid from an evaporator using rectifier, discharging the waste liquid from the rectifier, returning the discharged liquid to saccharification/fermentation means, and distilling the liquid.
NOVELTY - Soil processing agent comprises whole plant, stalk, leaves, processed material or extract of Spiraea thunbergii, and dicyandiamide.    USE - The soil processing agent is useful as delayed release fertilizer (all claimed).    ADVANTAGE - The agent enables to mineralize organic fertilizer continuously and finally incorporated as fertilizer component to plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for delayed release fertilizer, which comprises the soil processing agent and organic fertilizer.
NOVELTY - Organic fertilizer comprises 40-45 wt.% of sludge, 20-25 wt.% of salt slurry, 15-20 wt.% of cassava residue, 5-10 wt.% of urea, 3-5 wt.% of potassium phosphate and 0.2-0.3 wt.% of borax .    USE - The organic fertilizer is useful for crops.    ADVANTAGE - The organic fertilizer improves the quality and yield of crops, and adjusts soil pH value.
NOVELTY - Organic fertilizer is prepared by mixing raw materials comprising 60-65 pts. livestock and poultry manure, 25-30 pts. rapeseed, 10-15 pts. raw wheat bran, 5-8 pts. microbial agents, 1-2 pts. peat and humic acids, and 5-10 pts. chemical fertilizer at 50-55 degrees C, and stacking the mixture and composting the mixture for 11-13 days, where the microbial agents are amylase, protease, lipase or cellulase.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer can shorten composting time, and is nontoxic and environmentally-friendly, and does not produce peculiar odor.
NOVELTY - The equipment (1) has an inlet port (10) in which waste food is supplied. A reaction chamber (20) is arranged at lower end of the inlet port. The reaction chamber is provided to perform solid composting reaction in waste food accommodated in the inlet port. A knife-edged mixer is installed in the reaction chamber. A vacuum pump is connected to lower end of the reaction chamber. An odor reducing unit (40) is arranged at lower end of the reaction chamber for collecting odor generated during reaction process of food waste within the reaction chamber.    USE - Domestic waste food composting equipment.    ADVANTAGE - The generation of odor during reaction process of food waste within the reaction chamber can be prevented effectively, since odor reducing unit is arranged at lower end of reaction chamber for collecting odor generated during reaction process of food waste within the reaction chamber. The content in waste food can be removed. The odor reduction function of composting equipment can be improved. The operating efficiency of composting equipment can be improved. The harmful insect prevention effect and water pollution-resistant effect of composting equipment can be improved. The treatment period of food waste can be reduced. The composting equipment is environment-friendly. The generation of effluent can be reduced. The application rate of composting equipment can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a domestic waste food composting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the domestic waste food composting equipment.    Domestic waste food composting equipment (1)    Inlet port (10)    Reaction chamber (20)    Control unit (30)    Odor reducing unit (40)
NOVELTY - The method involves supplying waste and removing converted products. The waste is heated and biogas is removed during drop in pressure of gaseous medium in a reactor. The biogas is concentrated by methane at artificially predetermined modes corresponding to geophysical factors of ground such as pressure of gaseous medium, electromagnetic fields, the activity of water and gravity. The passage of microorganisms is boosted to the circadian rhythm of vital activity. The composition is formed over drain level.    USE - Method for processing organic waste.    DETAILED DESCRIPTION - The method involves extending composition periodically through the layer of drains in the methane-forming chamber participating in the reaction of methane formation. The drains are mixed and are conducted through the convector. The change in amplitude and frequency of vibrational movement of the parameters within natural vibration frequency of living cell is determined. An INDEPENDENT CLAIM is included for a device for processing of organic waste has bore container that is connected with reactor and is provided with a immobilization device and enricher of biogas. The reactor is provided with magnetic unit, heaters and convectors arranged to coaxially methane-forming chambers. The immobilization device is made from gas pyrrolidone water-permeable material. Multiple longitudinal threads arranged under the gas-water permeable material and are fixed to bottom portion of chamber. The threads are fixed to float component and are connected with top of methane-forming chamber by flexible element. The displacement of immobilization device is limited on vertical line downward.
NOVELTY - Preparing imidazole ionic liquid gel supported liquid membrane, comprises (i) preparing imidazole ionic liquid gel by adding 1-10 wt.% gel factor into imidazole ionic liquid, stirring at room temperature, grinding or ultrasonically processing for 5-60 minutes to obtain the product; and (ii) preparing ionic liquid gel supported liquid membrane by performing dipping method or pressing method of the imidazole ionic liquid gel includes filling imidazole ionic liquid gel into porous supporting material to obtain product.    USE - The membrane is useful for separation of gas, preferably mixed gas including carbon dioxide, sulfur dioxide, hydrogen, nitrogen, methane, carbon monoxide and any component in air (all claimed).    ADVANTAGE - The membrane has good separation effect, and stability.
NOVELTY - Preparing organic biofertilizer, involves (a) adjusting pH value of culture medium suitable for growth of microorganisms, subjecting culture solution to flash sterilization, and adding the sterilized culture solution to fermentation tank, (b) passing a portion of decanted water to mix tank, where remaining slurry is introduced into center of dryer, and materials are mixed with organic supplement culture medium and bacterial culture, and (c) drying the product, granulating the product, and packing the product.    USE - The method is useful for preparing organic biofertilizer (claimed).    DETAILED DESCRIPTION - Method for preparing organic biofertilizer, involves (a) adjusting pH value of culture medium suitable for growth of microorganisms, subjecting culture solution to flash sterilization, and adding the sterilized culture solution to fermentation tank, where stirring is continuously carried out, each fermentation tank comprises one or more strain, and contents of the fermentation tank are concentrated in a settling tank, (b) passing a portion of decanted water to mix tank, where remaining slurry is introduced into center of dryer, and materials are mixed with organic supplement culture medium and bacterial culture, and (c) drying the product, granulating the product, and packing the product.
NOVELTY - 5-(4-Fluorophenyl)-5-oxo-pentanoic acid is dissolved in anhydrous inert solvent in presence of catalyst under inert gas protection. Carbodiimide dehydrating agent and (4S)-4-phenyl-2-oxazolidinone are added into the mixture. The mixture is refluxed at 25-150 degrees C, reacted, cooled to room temperature and filtered. The filtrate is atmospheric or vacuum distilled to obtain yellow oil residue. Mixture of isopropanol and isopropyl ether is added into the residue, stirred and crystallized to obtain (4S)-3-(5-(4-fluorophenyl)-1,5-dioxo-pentyl)-4-phenyl-2-oxazolidinone.    USE - Manufacture of (4S)-3-(5-(4-fluorophenyl)-1,5-dioxo-pentyl)-4-phenyl-2-oxazolidinone used as intermediate for manufacturing ezetimibe.    ADVANTAGE - The method is simple, economical and environmentally-friendly.
NOVELTY - A Aspergillus niger strain pf1 (GMCC NO.7600), is new.    USE - In microorganism microbial inoculums; and for preparing microbial fertilizer (claimed).    ADVANTAGE - The Aspergillus niger strain improves utilization rate of the fertilizer; improves soil structure; increases yield and quality of crops.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) a microorganism microbial inoculums comprising the Aspergillus niger strain; and 2) preparing microbial fertilizer involving preparing Aspergillus niger strain using strain seed liquid pf1; inoculating the seed liquid to the solid culture medium, at 28 degrees C in culture medium; and culturing the culture into a sterile water, filtering, concentrating the filtrate to fermentation culture medium, at room temperature, and at relative humidity of more than 85% in fermentation chamber to ferment, where the culture medium is composed of solid and inorganic salt solution having mass ratio of 1:1.8, where the inorganic salt solution comprises 3.5% potassium dihydrogen phosphate, 0.04% magnesium sulfate, and 4% ammonium sulfate.
NOVELTY - Producing an alcohol comprises: providing a fermentable sugar produced by a method comprising contacting a biomass substrate with a recombinant beta-glucosidase polypeptide variant having beta-glucosidase activity; contacting the sugar with a fermenting microorganism; and recovering the produced alcohol. The recombinant beta-glucosidase polypeptide variant comprises an amino acid sequence that has at least 85% identity to SEQ ID NO: 4 (comprising fully defined 663 amino acids, as given in the specification) and comprises a substitution or deletion of the amino acid residue Phe-211.    USE - The method is useful for producing an alcohol that is ethanol (claimed).    ADVANTAGE - The method utilizes a recombinant beta-glucosidase polypeptide variant that has improved thermoactivity and low pH tolerance, compared to the wild type enzyme, and exhibits good tolerance to glucose.
NOVELTY - The system has multiple microwave output balls that are arrayed on a floor surface (3) of a fertilizer raw material integration bath (1) which is accumulated with fertilizer raw material. A microwave oscillating unit (19) outputs the microwave to a microwave waveguide (15) which propagates the microwave in the inner portion of integrated fertilizer raw material in the fertilizer raw material integration bath. The fertilizer raw material is heated by outputted microwave absorbed into moisture contained in fertilizer raw material and is converted into thermal energy.    USE - System for manufacturing compost such as cow dung, pig dung, hen droppings and food waste.    ADVANTAGE - The fertilizer raw material can be heated up efficiently by outputted microwave absorbed into the moisture contained in the fertilizer raw material. The power consumption and the manufacturing cost of the compost manufacturing system can be reduced. The activation environment can be optimized during manufacturing of compost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a compost manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compost manufacturing system.    Fertilizer raw material integration bath (1)    Floor surface of fertilizer raw material integration bath (3)    Microwave waveguide (15)    Microwave oscillating unit (19)    Ventilation pipe (21)
NOVELTY - The equipment has procedure eunuch (30) that is installed at the fermenter (16). An input unit is provided for committing the owner of the solid content formed in the upper portion of the compost fermentation tub (20). An exhausting unit ejects the compost by completing fermentation in the one-side wall of the compost fermentation tub. A pipe line is connected to the processing procedure eunuch installed in the lower unit of the compost fermentation tub. The solid content and the liquid are separated from solid through the solid-liquid separator (10).    USE - Compost ferment equipment used in undercurrent facility, digestive treatment facility, oxidation process facility, disinfection facility, sludge treatment facility etc.    ADVANTAGE - The production run reduction and productivity of the completely decomposed manure are heightened while the consumption of the humidity adjusting agent including sawdust or the rice hulls etc. is decreased by accelerating the moisture evaporation of the solid content error stored in the compost fermentation tub.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the compost ferment equipment.(Drawing includes non-English language text)    Solid-liquid separator (10)    Water storage tank (12)    Fermenter (16)    Compost fermentation tub (20)    Procedure eunuch (30)
NOVELTY - Production of ammonium phosphate comprises preparing phosphoric acid and removing sulfate. The method is performed by reacting raw materials of phosphorite slurry, reaction product of phosphoric acid, sulfate ion and calcium ion to form gypsum (CaSO4.2H2O) precipitate, removing phosphoric acid in sludge by precipitating, separating solid phase phosphate slurry, gypsum and phosphoric acid to obtain sulfate ion-free precipitate and ammonium phosphate, introducing phosphoric acid for ammonium phosphate production and depositing to form sludge for preparing phosphoric acid and recycling.    USE - Method for producing ammonium phosphate (claimed).    ADVANTAGE - The method reduces consumption of ammonia, improves quality of ammonium phosphate, recycles phosphate, reduces consumption of sulfuric acid consumption, increases production of phosphoric acid and conserve resources.
NOVELTY - Bio-organic fertilizer comprises 38-42 wt.% chicken manure with moisture content of not greater than 35%, 8-12 wt.% crop straw, 8 wt.% rice straw, 5 wt.% peanut hulls, 4 wt.% sawdust, 8 wt.% rice bran, 10 wt.% lees, 5 wt.% starch, 3 wt.% cork tree, 3 wt.% vetch, 2 wt.% fermentation agent, 0.4 wt.% cellulolytic bacteria, 0.4 wt.% semi-cellulolytic bacteria, 0.2 wt.% proteolytic bacteria, 0.2 wt.% organic phosphorus decomposing bacteria, 0.2 wt.% ammoniated fungus, 0.1 wt.% bioluminescent bacteria, 0.3 wt.% yeast and 0.2 wt.% actinomycetes.    USE - Bio-organic fertilizer used for improving physicochemical property and increasing bacterial content of soil.    ADVANTAGE - The fertilizer is low-cost, odorless and convenient to use.    DETAILED DESCRIPTION - Bio-organic fertilizer comprises 38-42 wt.% chicken manure with moisture content of not greater than 35%, 8-12 wt.% crop straw, 8 wt.% rice straw, 5 wt.% peanut hulls, 4 wt.% sawdust, 8 wt.% rice bran, 10 wt.% lees, 5 wt.% starch, 3 wt.% cork tree, 3 wt.% vetch, 2 wt.% fermentation agent, 0.4 wt.% cellulolytic bacteria, 0.4 wt.% semi-cellulolytic bacteria, 0.2 wt.% proteolytic bacteria, 0.2 wt.% organic phosphorus decomposing bacteria, 0.2 wt.% ammoniated fungus, 0.1 wt.% bioluminescent bacteria, 0.3 wt.% yeast and 0.2 wt.% actinomycetes. The fertilizer is prepared by mixing chicken manure, cellulolytic bacteria, semi-cellulolytic bacteria and proteolytic bacteria, fermenting for 6-8 days, adding organic phosphorus decomposing bacteria, ammoniated fungus, bioluminescent bacteria, yeast and actinomycetes, mixing and fermenting for 7-9 days; mixing crop straw, rice straw, peanut hulls, sawdust, rice bran, lees, starch, cork tree and vetch, pulverizing, placing in fermentation tank, adding fermentation agent, mixing and fermenting for 16-18 days; and taking out prepared raw materials, mixing, drying to obtain moisture content of not greater than 25%, blending, pelletizing and drying at 36-40 degrees C.
NOVELTY - Organic fertilizer with vegetable plant residues is prepared by taking vegetable plant leaves and roots, drying to obtain moisture content of 60-80%, pulverizing at 5-10 mesh, mixing with manure at ratio of 1-3:5, adding 0.1-0.5 wt.% microbial agents, mixing, fermenting at 60-80 degrees C with humidity of 50-70% for 3-5 days and stirring once every 12 hours.    USE - Method for preparing organic fertilizer with vegetable plant residues (claimed).    ADVANTAGE - The method is simple, low-cost and environment-friendly.    DETAILED DESCRIPTION - Organic fertilizer with vegetable plant residues is prepared by taking vegetable plant leaves and roots, drying to obtain moisture content of 60-80%, pulverizing at 5-10 mesh, mixing with manure at ratio of 1-3:5, adding 0.1-0.5 wt.% microbial agents, mixing, fermenting at 60-80 degrees C with humidity of 50-70% for 3-5 days and stirring once every 12 hours. Manure has moisture content of 40-60% and pH value of 6.5-7.5. Microbial agents comprise beer yeast, Bacillus subtilis, Lactobacillus delbrueckii, Streptomyces and mixture of Penicillium, oxalic acid and bentonite at ratio of 2-3:2-3:2-3:2-3:10-15.
NOVELTY - Kitchen waste for raw material of biological organic fertilizer is processed by taking kitchen waste, crop straw and chicken manure, mixing, inoculating solid state fermentation bacteria, drying at low temperature, and crushing. Bacteria is Bacillus subtilis ssp. natto, Bacillus subtilis or Candida tropicalis culture liquid.    USE - Method for processing kitchen waste for raw material of biological organic fertilizer (claimed).    ADVANTAGE - The fertilizer has improved fertilizing frame and quality. The process is safe and environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for (1) composition of biological organic fertilizer raw material comprising 40 wt.% kitchen waste, 30 wt.% crop straw, 30 wt.% chicken manure and 5 wt.% solid state fermentation bacteria inoculum; (2) preparation of biological organic fertilizer comprising weighing raw materials, mixing, adjusting moisture content to 45-55%, adding Bacillus subtilis ssp. natto and Bacillus subtilis with weight ratio of 1:1, fermenting for 24 hours, inoculating Candida, continuing fermentation at 42-48 degrees C, turning every 6 hours until isothermal, drying, and crushing; and (3) application of biological organic fertilizer comprising (A) digging groove or pit, scattering fertilizer, and transplanting seed; (B) applying additional fertilizer, dressing side ditch, and applying farmyard manure to replace chemical fertilizer; and (C) preprocessing, and maintaining soil moisture. Biological organic fertilizer and dressing application amounts are 140-200 kg/acre and 50-100 kg/acre, respectively.
NOVELTY - Manufacture of flower nutrient soil comprises crushing rice to diameter of less than 3 mm, dissolving 2 kg urea in 60 kg water, uniformly mixing, fermenting with 1.5 kg Oldham-enriched fermenting agent, mixing rice bran, adding material, stirring uniformly, adding water to maintain material humidity at 50%, and fermenting with thin film at 20-55 degrees C for 20 days to produce breeding nutrient soil.    USE - Method of production of flower nutrient soil used in flower planting (claimed).
NOVELTY - A potassium fulvate biological fertilizer comprises 150 g potassium fulvate, 50 g humus soil, 75 g copper sulfate, 75 g ferrous sulfate, 100 g zinc sulfate, 150 g manganese sulfate, 15 g ammonium sulfate, 10 g ammonium nitrate, 5 g magnesium chloride, 10 g potassium chloride, 20 g urea, 1 g boric acid, 2 g rare earth, 1 g vegetable protein, 2 g chitin and 10 g microbial inoculum. Biological fertilizer is prepared by making microbial inoculum, mixing at volume ratio of 3:2:1:1, weighing raw materials, adding 2 times amount of water, stirring, drying, and granulating.    USE - Potassium fulvate biological fertilizer for coloring and freeze-proofing fruit (claimed), strengthening disease resistance, insect resistance and drought resistance.    ADVANTAGE - The fertilizer has good frost resistance, long shelf life, simple preparation method, improved response rate, increased soil probiotic activity, and improved nutrient absorption, utilization and quality.    DETAILED DESCRIPTION - A potassium fulvate biological fertilizer comprises 150 g potassium fulvate, 50 g humus soil, 75 g copper sulfate, 75 g ferrous sulfate, 100 g zinc sulfate, 150 g manganese sulfate, 15 g ammonium sulfate, 10 g ammonium nitrate, 5 g magnesium chloride, 10 g potassium chloride, 20 g urea, 1 g boric acid, 2 g rare earth, 1 g vegetable protein, 2 g chitin and 10 g microbial inoculum. Biological fertilizer is prepared by taking Bacillus mucilaginosus broth, Bacillus subtilis broth, Lactobacillus broth and Streptomyces broth, mixing at volume ratio of 3:2:1:1, weighing raw materials, adding 2 times amount of water, stirring, drying, and granulating.
NOVELTY - A special fertilizer comprises compost, green manure, ash, humic acid fertilizer, microbial fertilizer, and light carbon mixture. The compost comprises straw, and human and animal excrement accumulation. The green manure is green plant nutrient fertilizer. The ash comprises plant ash, straw ash and rice husk ash. The humic acid fertilizer comprises cyclic amino acids. The microbial fertilizer is biofertilizer. The light carbon mixture is carbon dioxide absorbent.    USE - Special fertilizer used for mango (claimed).    ADVANTAGE - The fertilizer has low cost and good effect. After using, the mango tree has less disease, high nutrient absorption efficiency, and high fruit yield.
NOVELTY - An everolimus is purified by processing everolimus synthetic raw material using normal phase column chromatography to obtain greater than or equal to 95% pure crude everolimus, dissolving in aqueous organic solvent which is 1-3 carbon-containing alcohol or 4 carbon-containing ester, stirring at low temperature of about 5-10 degrees C, adding organic alkane, stirring until appearance of small crystals, performing ultrasonic crystallization which has isomer content of 1-5% that is measured using area normalization method, and filtering to obtain greater than or equal to 98% pure everolimus and less than or equal to 1% structural isomer.    USE - Purification of everolimus (claimed).    ADVANTAGE - Process blocks pathway to everolimus isomer crystal conversion, reduce impurities, has good crystallization effect, high yield, low cost, and low equipment requirement.    DETAILED DESCRIPTION - An everolimus is purified by processing everolimus synthetic raw material using normal phase column chromatography to obtain greater than or equal to 95% pure crude everolimus, dissolving in aqueous organic solvent which is 1-3 carbon-containing alcohol or 4 carbon-containing ester, stirring at low temperature of about 5-10 degrees C, adding organic alkane to everolimus solution, stirring until appearance of small crystals, performing ultrasonic crystallization which has isomer content of 1-5% that is measured using area normalization method, and filtering to obtain greater than or equal to 98% pure everolimus of formula (I) and less than or equal to 1% structural isomer of formula (II).    DESCRIPTION OF DRAWING(S) - The drawing shows a process steps of everolimus purification. (Drawing includes non-English language text).
NOVELTY - A methanol-gasoline blended fuel for car contains methanol, gasoline, and additive with volume ratio of 15-100:0-85:1-2 in which additive contains co-solvent, antiknock agent, lubricant, preservative, cleaning agent, combustion improver, and anti-vapor lock agent with volume ratio of 4-10:50-70:5-20:1-10:3-15:1-8:1-8.    USE - Methanol-gasoline blended fuel for car (claimed).    ADVANTAGE - The methanol-gasoline blended fuel is low cost, suitable for industrialized production, prevents oxidative corrosion, has excellent miscibility with methanol-cosolvent, strong dynamic property, complete combustion, high antiknock property, and no air resistance.
NOVELTY - A soil covering material comprises 2000-20000 pts. wt. cultivating soil, 125-200 pts. wt. dry livestock manure, 150-200 pts. wt. wheat shell or rice chaff, 10-20 pts. wt. lime, 20-30 pts. wt. calcium superphosphate and 3-5 pts. wt. dried microbial inoculum. Dried microbial inoculum contains live Pseudomonas putida.    USE - Soil covering material for promoting growth of Agaricus bisporus (claimed).    ADVANTAGE - The material increases mushroom production volume. The method is convenient, low-cost and labor-saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soil covering material comprising selecting cultivating soil, turning, crushing, mixing all components except inoculum, watering, adding dried microbial inoculum, mixing, and fermenting for 25-35 days.
NOVELTY - An industrial furnace radiant section modular device comprises furnace radiant section shell, and furnace radiant section tube set system in which radiant section furnace tube set is assembled in radiant section shell.    USE - Industrial furnace radiant section modular device for ethylene-ethane cracking furnace, hydrogen furnace, reformer furnace, and heating furnace.    ADVANTAGE - Device is easy to assemble, and has rational structure and reliable design.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a hydrogen furnace.
NOVELTY - Refining dihydroquercetin from larch by injection molding method, involves: 1) crushing the raw material of larch wood, adding aqueous ethanol solution, extracting, collecting the extracted solution and concentrating to obtain extract; 2) separating the extract having less MCI resin adsorption, carrying out gradient elution of the liquid phase of 0-30% aqueous ethanol solution as eluent, collecting 20-25 vol.% eluting component, concentrating and drying to obtain the quercetin crude product; and 3) re-crystallizing the quercetin crude product, and refining to obtain the dihydroquercetin.    USE - For refining dihydroquercetin from larch by injection molding method (claimed).    ADVANTAGE - The method uses water and ethanol as a solvent which has no pollution and can be recycled, uses adsorbent pore resin to introduce impurities; obtain product having purity of higher than 99%, contains no toxic component residue, uses pharmaceutical grade raw material; is simple, economic and environment-friendly; and is suitable for industrial production.
NOVELTY - Planting method of loquat comprises transplanting seedling to appointed position, culturing branch, entering flower fruit period, building greenhouse; opening sun-shading net anti-frost; thinning hanging fruit period, adding fertilizer to promote fruit; opening film door of shed; watering to root of tree crown, covering with film, and fruit picking.    USE - Planting method of loquat.    ADVANTAGE - The method prevents frost, rain crack fruit, and daily high temperature anti-burning.    DETAILED DESCRIPTION - Planting method of loquat comprises transplanting seedling to appointed position, where planting density is 3-5x 2-4 m, transplanting for 2-4 months, preferably 3 months; transplanting 25-50 cm lateral branches after sprouting year, culturing three year half branch, entering flower fruit period, building greenhouse, when winter and temperature is lower than 0 degrees C, covering whole heat preservation, when temperature is higher than 0 degrees C, lifting skirt film; opening sun-shading net anti-frost until returning to 2 degrees C; thinning hanging fruit period, adding fertilizer to promote fruit; opening film door of shed; watering to root of tree crown for 2-3 days, and covering with film, where sufficient temperature is higher than 30 degrees C, and fruit picking. An INDEPENDENT CLAIM is included for greenhouse comprising hot galvanized steel pipe connected with each other to form shed frame (1) with roll film (2), and skirt (3). The skirt is connected with shed frame and film (8). The retractable canopy frame is connected with vertically extending support pipe (4) with frame (5) having sun-shading net (7) and scroll film (6).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of greenhouse.    Shed frame (1)    Roll film (2)    Skirt (3)    Support pipe (4)    Frame (5)    Scroll film (6)    Sun-shading net (7)    Film (8)
NOVELTY - Processing dead livestock and poultry, comprises transporting dead livestock and poultry to treatment workshop, spraying disinfectant, sterilizing, cutting and crushing in deforming crusher, bubble spraying washing and sterilizing the obtained solid material, introducing the waste generated in cutting and crushing process to marsh gas fermentation tank, performing solid-liquid separation on the obtained solid-liquid mixture, processing solid material in organic fertilizer, subjecting liquid through oil-water separation, and taking oil separated from oil-water separation to produce biodiesel.    USE - The method is useful for processing dead livestock and poultry (claimed).    ADVANTAGE - The method is suitable for safe disposal of dead livestock, and simultaneously capable of generating energy for utilization and fertilizer.    DETAILED DESCRIPTION - Processing dead livestock and poultry, comprises: (a) collecting dead livestock and poultry using a collecting vehicle, transporting to a harmless treatment workshop, and spraying disinfectant, (b) sterilizing the dead livestock and poultry with hot water, introducing into a deforming crusher to carry out cutting and crushing, (c) bubble spraying washing the obtained solid material at high temperature and performing retort sterilization, introducing the waste generated in the cutting and crushing process to a marsh gas fermentation tank to perform marsh gas fermentation, (d) subjecting the sterilized solid-liquid mixture through solid-liquid separation, (e) processing the solid material in an organic fertilizer, and subjecting the liquid through oil-water separation, (f) taking the oil separated from the oil-water separation to produce biodiesel, and introducing the wastewater separated from the oil-water separation into the marsh gas fermentation tank of step (c) to perform marsh gas fermentation.
NOVELTY - The fertilizer has fresh beaver rabbit excrement mixed with ferment bacteria. Ferment powder potassium phosphate is mixed with the fresh beaver rabbit excrement, 5 parts of dolomite powder, 0.5 parts of borax, 0.2 parts of copper sulfate, 0.1 of zinc sulfate parts, 0.2 parts of manganese sulfate and 0.2 parts of photosynthetic solution. Buffer solution is contained with 0.67 wt.% photosynthetic bacteria water solution and 0.2 wt.% brown sugar. Fermentation temperature is controlled to about 55-70 degrees centigrade.    USE - Non-polluted farm biological organic and inorganic compound fertilizer.    ADVANTAGE - The fertilizer has high nutrition level, prolonged service life, high absorption rate and high utilization rate, and accelerates nutrient circulation decomposition level, improves soil permeability, and ensures better photosynthesis effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a non-polluted farm biological organic and inorganic compound fertilizer preparing method.
NOVELTY - Biological degradation treatment of animal decomposing body is carried out by putting animal decomposing body in a sealed container; setting temperature in the sealed container for sterilizing the body; putting fermentation bacteria to the sealed container and fermenting the decomposing body to obtain organic fertilizer primary product; and drying the biological organic fertilizer primary product in the sealed container to obtain organic fertilizer.    USE - Method for biological degradation treatment of animal decomposing body (claimed).    ADVANTAGE - The method does not cause secondary pollution to the environment.
NOVELTY - A biological fertilizer comprises 0.1-0.2 pts. wt. fermentation bacteria, 0.1-0.2 pts. wt. bacteriophage, 0.1-0.2 pts. wt. Magnetospirillum gryphiswaldense powder, 0.1-0.2 pts. wt. Beauveria bassiana powder, 0.1-0.2 pts. wt. Metarhizium anisopliae, 20-35 pts. wt. peat, 40-55 pts. wt. chicken manure, 15-35 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 14-24 pts. wt. bean straw, 5-9 pts. wt. potato straw, 0.1-0.3 pts. wt. lactic acid bacteria powder, 0.1-0.4 pts. wt. nitrifying bacteria powder, and 0.1-0.2 pts. wt. Rhizobium powder.    USE - Biological fertilizer used for increasing immune function of plants, promoting plant growth, improving soil condition, and inhibiting bacterial growth in the soil.
NOVELTY - An organic biofertilizer comprises 0.1-0.2 pts. wt. nitrogen-fixing bacteria powder, 0.1-0.2 pts. wt. Bacillus cereus powder, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 25-30 pts. wt. rice straw, 20-35 pts. wt. peat, 40-55 pts. wt. chicken manure, 15-35 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 14-24 pts. wt. bean straw, 5-9 pts. wt. potato straw, 0.1-0.3 pts. wt. lactic acid bacteria powder, 0.1-0.4 pts. wt. nitrifying bacteria powder, and 0.1-0.2 pts. wt. Rhizobium powder.    USE - Organic biofertilizer.    ADVANTAGE - The organic biofertilizer can improve quality and organic matter content of soil and suppress soil-borne disease, and has low cost, simple formulation, and no residue and no pollution.
NOVELTY - Agricultural organic fertilizer is prepared by adding Nocardia, Bacillus megaterium, Lactobacillus plantarum, thermophilic Bacillus licheniformis, and green Trichoderma strains to a fermentation tank, and adding strain culture medium and mixing to obtain composite microbial inoculum; adding adsorption carrier comprising wheat straw into microbial inoculum to obtain fermentation material; and stacking the fermentation material, inoculating, and fermenting the stack at 58-72 degrees C for 25-35 days to obtain the organic fertilizer.    USE - Method of preparing agricultural organic fertilizer (claimed) used for increasing crop disease resistance and improving soil structure.    ADVANTAGE - The method can promote straw recycling and improve quality of fertilizer product.    DETAILED DESCRIPTION - Preparation of agricultural organic fertilizer comprises: (A) respectively screening, separating, and purifying Nocardia, Bacillus megaterium, Lactobacillus plantarum, thermophilic Bacillus licheniformis, and green Trichoderma strains, and then transferring strains to a fermentation tank, and adding strain culture medium and mixing to obtain composite microbial inoculum; (B) adding adsorption carrier comprising wheat straw into microbial inoculum at less than 28 degrees C and adjusting water content to less than 30% to obtain fermentation material; and (C) stacking the fermentation material, adjusting water content to 55-65% and inoculating, and fermenting the stack at 58-72 degrees C for 25-35 days and turning every other day to obtain the organic fertilizer.
NOVELTY - A green microorganism fertilizer comprises 80-120 pts. wt. rice straw, 50-60 pts. wt. corn straw, 30-40 pts. wt. bean straw, 10-25 pts. wt. potato straw, 15-28 pts. wt. chicken manure, 20-35 pts. wt. pig manure, 20-35 pts. wt. calcium biphosphate, 1-3 pts. wt. partial phosphate, 2-8 pts. wt. potassium dihydrogen phosphate, 1-3 pts. wt. diammonium phosphate, 1-3 pts. wt. calcium biphosphate, 1-2 pts. wt. monocalcium phosphate, 1-2 pts. wt. boric acid.    USE - Green microorganism fertilizer.    ADVANTAGE - The fertilizer is non-toxic and harmless without pollution. It can provide nitrogen, phosphorus, potash fertilizer to crops, avoids compaction of soil, improves soil structure, and has strong heat water, especially for dry land crops effect which is better and longer.
NOVELTY - A high crop fertility biological fertilizer comprises 50-60 pts. wt. rice straw, 25-35 pts. wt. corn straw, 14-36 pts. wt. soyabean straw, 10-18 pts. wt. potato straw, 21-35 pts. wt. chicken manure, 10-15 pts. wt. duck manure, 4-6 pts. wt. diammonium phosphate, 3-8 pts. wt. manganese, 0.01-0.02 pts. wt. silicate bacteria, 0.01-0.02 pts. wt. Bacillus cereus, 0.01-0.02 pts. wt. Bacillus, 25-30 pts. wt. flour, 25-30 pts. wt. chicken manure, 14-25 pts. wt. rice bran, 10-16 pts. wt. wheat bran.    USE - High crop fertility biological fertilizer.    ADVANTAGE - The fertilizer has balanced nutrition and meets growth need of nutrient, has accelerated degradation to organic fertilizer, has low investment and high output value and improves quality of crop.
NOVELTY - Biological fertilizer comprises 0.1-0.2 pt. wt. Azotobacter powder, 0.1-0.2 pt. wt. Bacillus cereus powder, 0.1-0.2 pt. wt. Bacillus thuringiensis powder, 25-30 pts. wt. rice straw, 40-50 pts. wt. corn stover, 1-2 pts. wt. humic acid, 35-45 pts. wt. peat, 20-35 pts. wt. starch, 15-25 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 5-10 pts. wt. potato, 5-10 pts. wt. sucrose, 1-3 pts. wt. sodium chloride, 2-8 pts. wt. boric acid and 1-3 pts. wt. ammonium formate.    USE - Biological fertilizer used for improving soil fertility (claimed) and quality of crops.    ADVANTAGE - The fertilizer is simple, low-cost and environment-friendly.
NOVELTY - An agricultural controlled-release biological composite fertilizer comprises ammonium nitrate, calcium nitrate, potassium mineral powder, limestone powder, peat powder, caterpillar fungus powder, Bacillus popilliae powder, amino acids, Rhodococcus powder, steamed stuffed bun bacteria powder, Escherichia coli powder, Bacillus subtilis powder, pigweed cake, chicken manure, rice bran and rare earth fertilizer.    USE - Agricultural controlled-release biological composite fertilizer.    ADVANTAGE - The composite fertilizer has small water solubility, thus slowly releasing and reducing loss of nutrients in soil.    DETAILED DESCRIPTION - An agricultural controlled-release biological composite fertilizer comprises 1-3 pts. wt. ammonium nitrate, 2-6 pts. wt. calcium nitrate, 1-3 pts. wt. potassium mineral powder, 7-13 pts. wt. limestone powder, 25-35 pts. wt. peat powder, 0.1-0.2 pt. wt. caterpillar fungus powder, 0.1-0.2 pt. wt. Bacillus popilliae powder, 1-2 pts. wt. amino acids, 0.01-0.02 pt. wt. Rhodococcus powder, 0.01-0.02 pt. wt. steamed stuffed bun bacteria powder, 0.01-0.02 pt. wt. Escherichia coli powder, 0.01-0.02 pt. wt. Bacillus subtilis powder, 14-25 pts. wt. pigweed cake, 25-35 pts. wt. chicken manure, 14-23 pts. wt. rice bran and 1-2 pts. wt. rare earth fertilizer.
NOVELTY - A high-efficiency controlled-release biological organic composite fertilizer comprises ammonium nitrate, calcium nitrate, potassium mineral powder, limestone powder, peat powder, caterpillar fungus powder, Bacillus popilliae powder, ammonium dihydrogen phosphate, corn straw, soybean straw, calcium biphosphate, trimetaphosphoric acid, potassium biphosphate, potassium dihydrogen phosphate, diammonium hydrogen phosphate and boric acid.    USE - High-efficiency controlled-release biological organic composite fertilizer.    ADVANTAGE - The composite fertilizer has small water solubility, thus slowly releasing nutrients and reducing loss of nutrients in soil.    DETAILED DESCRIPTION - A high-efficiency controlled-release biological organic composite fertilizer comprises 1-3 pts. wt. ammonium nitrate, 2-6 pts. wt. calcium nitrate, 1-3 pts. wt. potassium mineral powder, 7-13 pts. wt. limestone powder, 25-35 pts. wt. peat powder, 0.1-0.2 pt. wt. caterpillar fungus powder, 0.1-0.2 pt. wt. Bacillus popilliae powder, 1-7 pts. wt. ammonium dihydrogen phosphate, 40-50 pts. wt. corn straw, 40-50 pts. wt. soybean straw, 10-15 pts. wt. calcium biphosphate, 1-3 pts. wt. trimetaphosphoric acid, 2-8 pts. wt. potassium biphosphate, 1-3 pts. wt. potassium dihydrogen phosphate, 1-3 pts. wt. diammonium hydrogen phosphate and 1-2 pts. wt. boric acid.
NOVELTY - A green microbial fertilizer comprises 0.1-0.2 pt. wt. bacterial enzymes, 0.1-0.2 pt. wt. bacteriophage powder, 0.1-0.2 pt. wt. Azospirillum powder, 0.1-0.2 pt. wt. Beauveria bassiana powder, 0.1-0.2 pt. wt. Metarhizium anisopliae powder, 3-7 pts. wt. potato, 1-3 pts. wt. sucrose, 1-7 pts. wt. agar, 70-95 pts. wt. corn straw, 55-75 pts. wt. bean straw, 25-35 pts. wt. potato straw, 1-8 pts. wt. phosphate rock powder and 2-7 pts. wt. oyster shell.    USE - Green microbial fertilizer used for promoting plant growth.    ADVANTAGE - The fertilizer improves soil condition by preventing growth of bacteria.
NOVELTY - A farmland microbial fertilizer comprises chicken manure, sweet potato powder, peat, calcium superphosphate, potassium sulfate, Bacillus sphaericus powder, rice straw, rice bran, amino acids, chitin, polypeptides, potassium polymetaphosphate, potassium pyrophosphate, sodium aluminum phosphate, calcium hydrophosphate, calcium phosphate, calcium pyrophosphate, humic acid and Verticillium powder.    USE - Farmland microbial fertilizer.    ADVANTAGE - The fertilizer has high content of nutrients needed by crops.    DETAILED DESCRIPTION - A farmland microbial fertilizer comprises 35-45 pts. wt. chicken manure, 10-15 pts. wt. sweet potato powder, 20-35 pts. wt. peat, 9-16 pts. wt. calcium superphosphate, 7-10 pts. wt. potassium sulfate, 0.1-0.2 pt. wt. Bacillus sphaericus powder, 35-45 pts. wt. rice straw, 30-40 pts. wt. rice bran, 1-2 pts. wt. amino acids, 0.5-1.0 pt. wt. chitin, 0.1-0.2 pt. wt. polypeptides, 3-7 pts. wt. potassium polymetaphosphate, 2-9 pts. wt. potassium pyrophosphate, 3-4 pts. wt. sodium aluminum phosphate, 1-6 pts. wt. calcium hydrophosphate, 2-6 pts. wt. calcium phosphate, 3-4 pts. wt. calcium pyrophosphate, 5-9 pts. wt. humic acid and 0.1-0.3 pt. wt. Verticillium powder.
NOVELTY - An agricultural quick-release microbial fertilizer comprises 20-35 pts. wt. peat, 15-20 pts. wt. urea, 12-15 pts. wt. ammonium sulfate, 5-9 pts. wt. potassium polymetaphosphate, 1-3 pts. wt. potassium pyrophosphate, 4-8 pts. wt. magnesium phosphate, 3-8 pts. wt. manganese phosphate, 12-24 pts. wt. sesame straw, 10-13 pts. wt. hemp straw, 14-25 pts. wt. sunflower straw, 0.1-0.3 pt. wt. Bdellovibrio bacteriovorus powder, 0.1-0.2 pt. wt. bacteriophage powder, 0.1-0.1-2 pt. wt. Oceanospirillales powder, 50-60 pts. wt. sewage sludge and 0.1-0.2 pt. wt. bacterial enzymes.    USE - Agricultural quick-release microbial fertilizer.    ADVANTAGE - The fertilizer has good water absorption property. It has high content of nutrients for growing plants and improving soil physical properties and fertility.
NOVELTY - A biological organic fertilizer comprises 395-405 pts. wt. nitrogen fertilizer, 85-95 pts. wt. phosphate fertilizer, 85-95 pts. wt. potash fertilizer, 405-420 pts. wt. alcohol production waste residue, 2.8-3.3 pts. wt. Bacillus mucilaginosus spore, and 2.8-3.3 pts. wt. Bacillus subtilis spore.    USE - Biological organic fertilizer used for corn (claimed).    ADVANTAGE - The organic fertilizer can provide corn leaf having deep green color with 2-3 sections, width of 3-5 mm, and length of 8 cm. The corn plant has height of 35-40 cm and diameter of 2.5 cm.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biological organic fertilizer, comprising mixing monosodium glutamate production waste residue as nitrogen fertilizer, alcohol production waste residue, powdered rock phosphate as phosphate fertilizer and potassium feldspar powder as potash fertilizer, adding Bacillus mucilaginosus spore and Bacillus subtilis spore, fermenting and increasing content of organic matter and humic acid, and pelletizing after fermenting.
NOVELTY - An ecological agriculture microorganism fertilizer comprises 80-120 pts. wt. rice straw, 50-60 pts. wt. corn straw, 30-40 pts. wt. bean straw, 10-25 pts. wt. potato straw, 15-28 pts. wt. chicken manure, 20-35 pts. wt. mustard rice stalk, 12-24 pts. wt. sesame rice stalk, 12-24 pts. wt. sesame stalk, 10-13 pts. wt. hemp stalk, 14-25 pts. wt. rice stalk, 0.1-0.3 pts. wt. sunflower stalk, 0.1-0.2 pts. wt. bacteria powder, 0.1-2 pts. wt. bacteriophage spirillum marine powder, 50-60 pts. wt. sludge, and 0.1-0.2 pts. wt. ferment fungus.    USE - An ecological agriculture microorganism fertilizer for dry-land crops.    ADVANTAGE - The fertilizer is safe and toxic-free, does not cause pollution, improves yield of crops, has strong resistance to heat and water, does not cause soil compaction, and has desired nitrogen, phosphorus, potash fertilizer content.
NOVELTY - 1-ferrocenyl-3-((N-(2-substituted benzimidazolyl)))-2-propen-1-one is new.    USE - 1-ferrocenyl-3-((N-(2-substituted benzimidazolyl)))-2-propen-1-one for preparation of anti-gram bacteria medicine for resisting Staphylococcus aureus, Escherichia coli, or Streptococcus (all claimed).    ADVANTAGE - Preparation process is simple and effective and has mild reaction conditions, short reaction time, good product yield, and no pollution.    DETAILED DESCRIPTION - 1-ferrocenyl-3-((N-(2-substituted benzimidazolyl)))-2-propen-1-one of formula (I) is new.    R=Me, Et, propyl, phenoxy methylene, or methylene oxide.    An INDEPENDENT CLAIM is included for preparation of 1-ferrocenyl-3-((N-(2-substituted benzimidazolyl)))-2-propen-1-one.
NOVELTY - This invention relates to a highly stable and efficient anode structure for solid oxide fuel cell and its manufacturing method. Its structure is formed by stacking a porous ventilation metal substrate, a diffused shielding film, and a nano-structure composite thin film through atmospheric plasma coating. The nano-structure composite thin film comprises a plurality of nano-metal powder particles, a plurality of nano-metal oxide powder particles, and a plurality of nano gas passages. The nano-metal powder particles are connected to form a three-dimensional network capable of conducting electrons. The nano-metal oxide powder particles are connected to form another three-dimensional network capable of conducting oxygen ions. Internet backbone formed by connecting the nano-metal oxide powder particles has enough strength, capable of isolating metal powder particles and effectively preventing metal powder particles from aggregating. It is suitable for applying in moderate and low temperatures working range with respect to solid oxide fuel cell.
NOVELTY - Disclosed is a method of using vegetable oil to prepare biodiesel, which includes: firstly obtaining an oil phase solution obtained by carrying out pre-esterification of vegetable oil, then heating the oil phase solution to reach a temperature of 60 DEG C to 85 DEG C by using a microwave heating method, adding a homogeneous alkaline catalyst and a first alcohol into the oil phase solution to obtain a transesterification solution, and separating a biodiesel from the transesterification solution after cooling the transesterification solution. The microwave heating method has advantages of fast heating, uniform heat transfer, etc., thereby capable of shortening the time of transesterification within 4 seconds to 30 minutes. In addition, the biodiesel finally obtained by this method has high conversion rate and selection rate. Thereby, this method can complete biodiesel production in shorter time period without sacrificing biodiesel quality.
NOVELTY - A biodiesel reactor comprises container (1), motor (2), speed reducer (3), stirring shaft (4), blade (5), feeding port A and B, observation hole, manhole, discharge port, inclined plane, spiral heating pipe, liquid inlet and outlet.    USE - Biodiesel reactor used for preparing biological diesel oil.    ADVANTAGE - The reactor has simple structure, low equipment cost and is convenient to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biodiesel reactor.    Container (1)    Motor (2)    Speed reducer (3)    Stirring shaft (4)    Blade (5)
NOVELTY - Processing waste substances, where organic constituents of the waste substances are expelled in a reactor, involves introducing the waste substances into the reactor; heating the waste substances under vacuum to a boiling temperature of water; applying shear forces to the waste substances received in the reactor via a stirring device; and destroying membranes of water-containing cell structures of the organic constituents and expelling of the engendered exhaust vapor containing organic constituents.    USE - The method is useful for processing waste substances, where organic constituents of waste substances are expelled in reactor (claimed).    ADVANTAGE - Stabilization of the residual waste may be carried out at reduced expense in terms of method and apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing plant for processing waste substances containing organic constituents, in particular for carrying out the method, comprising a heatable reactor capable of being taken under vacuum to a boiling temperature of water or of another leaching fluid, and having a waste substances inlet, a material discharge, a vacuum port, a heating, an exhaust vapor outlet and a means for the introduction of shear forces, in particular a stirring mechanism.
NOVELTY - A high-stability sulfur-resistant methanation catalyst comprises 5-25 pts. wt. molybdenum oxide (MoO3), 3-35 pts. wt. yttria (Y2O3), and 40-92 pts. wt. zirconia (ZrO2).    USE - High-stability sulfur-resistant methanation catalyst used for multistage methanation reaction, or last 1-2 stages of methanation reaction (claimed).    ADVANTAGE - The catalyst has high catalytic activity, stability, and hydrogen sulfide atmosphere, and low reverse water gas shift activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst by (A) subjecting ZrO2 to coprecipitation, deposition precipitation, or sol-gel method to prepare ZrO2 carrier or commercially ZrO2 carrier; (B) soaking in yttria solution; (C) drying, and calcining to obtain Y2O3-ZrO2 composite carrier; (D) soaking in MoO3 precursor solution to carry out deposition method; and (E) drying, calcining.
NOVELTY - A kitchen garbage molded fuel oil is prepared by sorting kitchen garbage, crushing, cleaning, removing impurities, heating to remove oil, performing deep dehydration of slag, separating oil in oil-water separator and hot air-drying dehydrated slag.    USE - Method for preparing kitchen garbage molded fuel oil (claimed).    ADVANTAGE - The method has high utilization rate of fuel energy and adopts recycling of heat from hot air.
NOVELTY - A refrigerant comprises 58.1-62.1 wt.% pentafluoroethane, 7.5-9.5 wt.% 1,1-difluoroethane, 25.5-29.5 wt.% 1,1,1,2-tetrafluoroethane, and 2.4-3.9 wt.% propane.    USE - Refrigerant used as hydrochlorofluorocarbon-22 (R22) substitute.    ADVANTAGE - The refrigerant has cooling effect close to R22 and is ozone-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of refrigerant comprising injecting pentafluoroethane, 1,1-difluoroethane, 1,1,1,2-tetrafluoroethane and propane in steel bottle and mixing raw materials.
NOVELTY - Production of calcium carbide comprises coking long strip-shaped biomass fuel, combusting powdered calcium and volatile oxygen-containing gas to produce calcium carbide and by product carbon dioxide as heating fuel, preheating powdered calcium-containing raw material using auxiliary fuel, coking biomass fuel of solid carbon, and mixing with powdered calcium-containing raw material.    USE - Method for producing calcium carbide (claimed).    ADVANTAGE - The system improves the utilization rate of raw material. The method has wide raw material sources, low coking temperature, large production capacity, and stable reactor temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the production system comprising raw material pre-heating unit, reaction unit, plasma ignition temperature control device, circulating fluidized bed reactor, calcium carbonate pre-heating unit, biomass pre-heating unit, feeder, heat exchanger, gas compression device, solid material inlet, solid material outlet, gas inlet, gas outlet, gas compression apparatus, solid material inlet, solid material outlet, solid material mixer, and biomass fuel pre-heater.
NOVELTY - A biomass fuel comprises 85-95 wt.% combustible biomass and 5-15 wt.% waste plastic powder. The combustible biomass is a forestry waste, crop straw, bean pod and/or nut shell. The waste plastic is polyethylene and/or polypropylene.    USE - Biomass fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biomass fuel, comprising crushing combustible biomass and then drying to water content of less than 10 wt.%; putting crushed biomass into a mixer and adding waste plastic powder and uniformly mixing them; and continuously extruding the mixture into strips at 20-50 MPa at 120-175 degrees C, then air cooling to room temperature, and packaging to obtain the biomass fuel.
NOVELTY - A municipal sludge and biomass derived fuel is prepared by respectively coarse crushing biomass raw material and municipal sludge, stirring and drying; adding crushed biomass material, crushed municipal sludge and additive into a crusher for fine crushing, stirring, drying; mixing the finely crushed materials, adding second additive, stirring and drying the mixture, then performing secondary fine crushing, stirring and drying; extruding the finely crushed materials and molding; and low-temperature drying the molded fuel material at 80-180 degrees C for 50-70 minutes to obtain the fuel.    USE - Method of preparing municipal sludge and biomass derived fuel (claimed).    ADVANTAGE - The method is energy-saving and suitable for industrialization and can realize zero discharge. The municipal sludge material does not need pre-baking or dehydration treatment.
NOVELTY - Domestic waste material derived fuel is prepared by crushing and screening domestic wastes comprising large block stone, brick, glass and metal; performing secondary crushing and magnetic separation; performing fine crushing, stirring, and drying crushed material, then adding additive powder, continuously crushing, uniformly mixing, and drying; spraying dried mixed material with 5-8% sodium hydroxide solution; adding mixed material with second additive, continuously crushing and stirring, extruding and molding; and drying molded material at low temperature of 80-180 degrees C for 50-70 minutes.    USE - Method of preparing domestic waste material derived fuel (claimed).    ADVANTAGE - The method utilizes high humidity waste material which does not need manual separation, dehydration and pre-baking steps, and can obtain fuel having sufficient combustion. Further, the method is energy-saving and can realize zero discharge.
NOVELTY - Municipal sludge derived fuel is prepared by crushing and screening domestic wastes comprising large block stone, brick, glass and metal; performing secondary crushing and magnetic separation; performing fine crushing, stirring, and drying crushed material, then adding additive powder, continuously crushing, uniformly mixing, and drying; adding mixed material with second additive, continuously crushing and stirring, extruding and molding; and drying molded material at low temperature of 80-180 degrees C for 50-70 minutes to obtain the fuel.    USE - Method of preparing municipal sludge derived fuel (claimed).    ADVANTAGE - The method is energy-saving and can realize zero discharge. It utilizes high humidity municipal sludge which does not need manual separation, dehydration and pre-baking steps.
NOVELTY - The hydrogen-separation liquid cooling system tank has two holes formed on the side of a cooling tank to receive round stainless steel pipes and rubber tubes for cooling liquid circulation which circulate heat generated from a hydrogen separation tank. A pump circulates cooling liquid to a car's radiator. A liquid cooling system tank lid has a cooling liquid refill pipe (2), a cooling liquid checking pipe (3) and an electrolyte solution level meter (16). The top and bottom of the hydrogen-separation liquid cooling system tank is welded to the hydrogen separation tank.    USE - Hydrogen-separation liquid cooling system tank for car engine.    ADVANTAGE - Reduces heat to stabilize direct current (DC) in electrolysis process. Produces hydrogen which can be used together with fossil fuel. Reduces toxic gases and carbon oxide gas from engine. Offers environmentally-friendly hydrogen-separation liquid cooling system tank.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the arrangement of cell plates and a permanent magnet connected to an anode shaft.    Cooling liquid refill pipe (2)    Cooling liquid checking pipe (3)    Anode shaft (9)    Cathode shaft (10)    Electrolyte solution level meter (16)
NOVELTY - The apparatus comprises a reactor equipped with a circulation line, a steam boiler, a drain trap for discharging condensed water, and a condensate storage tank. The steam is supplied to the reactor to raise a temperature of the circulation line.    USE - The apparatus is useful for producing a biodiesel (claimed).    ADVANTAGE - The apparatus has improved operational efficiency, and is capable of economically producing large amount of biodiesel in an environmentally friendly manner.
NOVELTY - An electrode has carbon nanotubes, a catalyst supported by carbon nanotubes, and an ionomer which coats the carbon nanotubes and catalyst. The length (La) of carbon nanotubes is 30-240 mu m. The length (La) of carbon nanotubes and center-to-center pitch (Pa) ( nu m) of carbon nanotubes satisfy a specific relation (I).    USE - Electrode is used for manufacture of membrane electrode assembly for manufacturing fuel cell (all claimed).    ADVANTAGE - The electrode has excellent power generation characteristics.    DETAILED DESCRIPTION - An electrode has carbon nanotubes, a catalyst supported by carbon nanotubes, an ionomer which coats the carbon nanotubes and catalyst. The length (La) of carbon nanotubes is 30-240 mu m. The length (La) of carbon nanotubes and center-to-center pitch (Pa) ( nu m) of carbon nanotubes satisfy a relation: 0.351x La+75 less than or equal to Pa less than or equal to 250 (I). INDEPENDENT CLAIMS are included for the following:    (1) manufacture of electrode;    (2) manufacture of membrane electrode assembly; and    (3) manufacture of fuel cell.
NOVELTY - Off-gas (2b) discharged from a hydrogen-gas manufacturing equipment (2) which uses coke oven gas as raw material and manufactures hydrogen (2a), is used as fuel in power stations (4). By charging off-gas to the gas holder (5) piping (5b) branched from the middle of power station coke-oven gas piping (4a), off-gas is stored and then discharged to the gas holder.    USE - Utilization of off-gas discharged from hydrogen-gas manufacturing equipment (claimed) which uses iron-mill by-product gas as raw material.    ADVANTAGE - The method enables effective usage of off-gas and production of electric power effectively during day with high electric-power unit price.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the piping system. (Drawing includes non-English language text)    Hydrogen-gas manufacturing equipment (2)    Hydrogen (2a)    Off-gas (2b)    Power station (4)    Coke-oven gas piping (4a)    Gas holder (5)    Gas holder piping (5b)
NOVELTY - A molded product is obtained by compression-molding molded porous article containing granular material and binder of biomass. The granular material of biomass contains granular material of bamboos.    USE - Molded product is used for solid fuel (claimed) and cleaning sources e.g. fertilizer source used in agriculture and water.    ADVANTAGE - The molded product has improved moldability and combustibility, and high lightweight and handleability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of molded product; and    (2) manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of pulverization unit.    Pulverization unit (1)    Rotation gear (2)    Rotating shaft (3)    Supply path (4)    Pulley (8)
NOVELTY - Generating a modified algal cell which shows increased productivity and/or improved resistance to programed cell death compared to a non-modified algal cell when maintained under identical conditions, comprises modifying the algal cell by down-regulating a metacaspase.    USE - The method is useful for generating a modified algal cell which shows increased productivity and/or improved resistance to programed cell death; producing plastic, detergent, non-toxic biodegradable polymer, animal feed, fertilizer, nutraceutical, pharmaceutical, biofuel and cosmetic (all claimed).    ADVANTAGE - The method is capable of modifying at least 40% of the algal cells having increased productivity (such as increased biomass and/or output of cellular products), thus achieving high product yield in algal populations.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a genetic construct comprising a nucleic acid molecule whose expression is capable of increasing the productivity of the cell and/or improving resistance to programed cell death compared to a cell which does not comprise the genetic construct; and    (2) a modified algal cell.
NOVELTY - The apparatus (20) has a monitoring unit (22) which monitors the treatment condition about the organic to-be-processed object in the biological reactor (10) or the treated water emitted from the biological reactor. A degassing unit (24) removes the dissolved gas which prevents biological treatment from the organic to-be-processed object in the biological reactor after measuring value of pH of the organic to-be-processed object in biological reactor, and measuring quantity of the substance in organic to-be-processed object.    USE - Dissolved-gas removal apparatus used in biological treatment apparatus (claimed) of organic to-be-processed object.    ADVANTAGE - The falling into rancid state in a biological reactor which biologically treats an organic to-be-processed object can be suppressed even without using the separation membrane having the high degree separation function, so that the generation of the methane gas can be performed stably at high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) the processing apparatus of organic to-be-processed object;    (2) the biological treatment apparatus of organic to-be-processed object; and    (3) the biological treatment method of organic to-be-processed object.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biological treatment apparatus.    Biological reactor (10)    Dissolved-gas removal apparatus (20)    Monitoring unit (22)    Degassing unit (24)    Biological treatment apparatus (100)
NOVELTY - Producing a synthetic gas rich in carbon monoxide (CO) and carbon dioxide (CO2) or a synthesis gas rich in hydrogen (H2) and CO from a biosolid having an initial solids content that does not exceed 30 wt.%, involves: (a) admixing the biosolid having an initial solids content that does not exceed 30 wt.% with a solid material that comprises tar-rich materials and/or char particles; (b) drying the mixture; and (c) partially oxidizing the mixture under conditions to produce a synthetic gas rich in CO and CO2 or a synthesis gas rich in H2 and CO.    USE - The method is useful for producing synthetic gas rich in CO and CO2 or synthesis gas rich in H2 and CO from biosolid having initial solids content that does not exceed 30 wt.% (claimed).    ADVANTAGE - A better method is provided for disposing of such biosolids, by converting them to a synthetic gas.    DETAILED DESCRIPTION - Producing a synthetic gas rich in carbon monoxide (CO) and carbon dioxide (CO2) or a synthesis gas rich in hydrogen (H2) and CO from a biosolid having an initial solids content that does not exceed 30 wt.%, involves: (a) admixing the biosolid having an initial solids content that does not exceed 30 wt.% with a solid material that comprises tar-rich materials and/or char particles to provide a mixture comprising the biosolid having an initial solids content that does not exceed 30 wt.% and the tar-rich materials and/or char particles; (b) drying the mixture where the mixture, after drying, has a solids content of at least 75 wt.%; and (c) partially oxidizing the mixture under conditions to produce a synthetic gas rich in CO and CO2 or a synthesis gas rich in H2 and CO.
NOVELTY - The set of even number of generators of gas by electrolysis of water for multiphase voltage has an inverter of phase supply into which direct unsmoothed multiphase voltage is supplied. A source of alternating multiphase voltage (8) is connected to the pulse switches (10) that are connected to a pulse generator (9). The pulse generator launches generated pulses into pulse switches that switch the multiphase voltage into the rectifiers (11) that are connected to the generators (12).    USE - Set of even number of generators of gas by electrolysis of water for multiphase voltage used for gas production.    ADVANTAGE - Provides an efficient and increased gas production while costs associated with the production is reduced through the use of multiphase voltage and structure of electrodes and a number of seal that is suitable for efficient electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows an electric connection of the generators which consist of source of multiphase alternating voltage, rectifier and generator.    Source of alternating multiphase voltage (8)    Pulse generator (9)    Pulse switches (10)    Rectifiers (11)    Generators (12)
NOVELTY - Grass plant, in which the expression of an endogenous XAX1 gene is genetically altered in comparison to a corresponding wild type grass plant that does not have the genetic alteration, is new. The genetic alteration decreases expression of the endogenous XAX1 gene.    USE - The grass plant is useful for obtaining a fiber preparation and improving the amount of soluble sugar obtained from grass plant biomass material (all claimed) for biofuel production, where the fiber preparation is useful in food materials for animals, including humans.    ADVANTAGE - The plant has: at least a 10% increase in sugar extractability; at least a 10% reduction in the level of hydroxycinnamate esters; and at least a 10% reduction in lignin content, compared to the corresponding wild type plant lacking the vector.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a plant cell from the plant;    (2) a seed, flower, leaf, stem, fruit or stalk from the plant;    (3) obtaining an increased amount of soluble sugars from a grass plant in a saccharification reaction, comprising inhibiting the expression of an endogenous XAX1 gene in the plant and incubating plant material from the plant in a saccharification reaction;    (4) altering the xylan content in a grass plant, comprising inhibiting expression of an endogenous XAX1 gene in the plant;    (5) improving the amount of soluble sugar obtained from grass plant biomass material, comprising providing plant biomass material from the grass plant in which endogenous XAX1 gene expression is inhibited, performing a saccharification reaction and obtaining soluble sugar;    (6) bulk harvested material comprising material from at least two engineered plants of the grass plant; and    (7) a saccharification reaction comprising grass plant biomass material from the grass plant in which endogenous XAX1 gene expression is inhibited.
NOVELTY - Producing at least one fluid hydrocarbon product from a hydrocarbonaceous material, comprises feeding a hydrocarbonaceous material to a reactor (20), and pyrolyzing within the reactor, in the presence of a solid catalyst, at least a portion of the hydrocarbonaceous material under reaction conditions sufficient to produce at least one gaseous pyrolysis product, condensing the gaseous pyrolysis products to form a liquid phase condensed product, and feeding a portion of the liquid phase condensed product to the reactor.    USE - The method is useful for producing at least one fluid hydrocarbon product from a hydrocarbonaceous material, where the hydrocarbonaceous material comprises a biomass material, plastic waste, recycled plastics, agricultural and municipal solid waste, food waste, animal waste, carbohydrates, lignocellulosic materials, xylitol, glucose, cellobiose, hemicellulose, lignin, sugar cane bagasse, glucose, wood, and/or corn stover (claimed).    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a system for pyrolysis of biomass with a liquid recycle step.    Reactor (20)    Regenerator (30)    Condenser (50)    Aqueous phase (84)    Organic phase (94)
NOVELTY - Degrading cellulose or lignocellulosic biomass, involves: contacting a cellulose containing material or lignocellulosic biomass with an enzyme cocktail comprising at least one fungal cellulase and at least one high molecular weight (HMW) cellulosome complex.    USE - For degrading cellulose or lignocellulosic biomass (claimed); for producing a biofuel from lignocellulosic biomass; and for degrading cellulose and materials containing cellulose using the enzyme cocktails which is used in compositions to help degrade (e.g. by liquefaction) a variety of cellulose products (e.g. paper, cotton, etc.) in landfills; and to enhance the cleaning ability of detergents, function as a softening agent or improve the feel of cotton fabrics (e.g. stone washing or biopolishing) or in feed compositions.    ADVANTAGE - The combinations of free fungal enzymes with cellulosomes show synergistic activities on cellulose-containing substrates. Typically, cellulosomes are more efficient at digesting crystalline cellulose, while the cellulosomes are not as effective as the free enzymes at degrading pretreated biomass, yet together the two systems are more efficient at cellulose degradation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) producing a biofuel from lignocellulosic biomass, involving: a) contacting the lignocellulosic biomass with the enzyme cocktail; and b) converting the sugars to a biofuel by fermentation; and    (2) an enzyme cocktail comprising at least one HMW cellulosome complex and a Family 7 cellobiohydrolase; and/or CTec2.
NOVELTY - Converting alcohol into fuel mixture comprising alcohol, ether and water, suitable for operating an internal combustion engine (5) of a motor vehicle, in a reactor (3), is claimed. The mixing ratio of alcohol, ether and water in the fuel mixture is adjusted by controlling at least one reaction parameter of a reaction occurring in the reactor.    USE - The fuel mixture is useful for operating an internal combustion engine (5) in a motor vehicle (claimed).    ADVANTAGE - The method produces the fuel mixture having high cetane number (preferably greater than 50) with consistent quality, and ensures the adjustment of the combustion properties in a simple manner by controlling the reaction temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device comprising the reactor for converting the heated alcohol into fuel mixture using a heating device (2), and a control device (10) for adjusting the heating of the alcohol in the heating device and/or the pressure in the reactor depending on the reaction parameters of the reaction occurring in the reactor and/or depending on the operating parameters of the internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for converting the alcohol into the fuel mixture.    Heating device (2)    Reactor (3)    Internal combustion engine (5)    Control device (10)    Exhaust gas heat exchanger (16)
NOVELTY - A stabilized visible-light responsible semiconductor electrode consists of protective film and semiconductor layer. The protective film comprises a compound containing an element chosen from niobium, tin, zirconium, lanthanum, titanium, bismuth, and tantalum. The semiconductor layer is formed by coating bismuth, vanadium, tungsten, and oxygen as a constituent element on a semiconductor.    USE - Stabilized visible-light responsible semiconductor electrode e.g. photoelectrode is used for reaction of aqueous solution containing carbonate electrolyte used in water splitting reaction apparatus (all claimed) used for production of hydrogen, and photosensors.    ADVANTAGE - The stabilized visible-light responsible semiconductor electrode has excellent stability and light energy conversion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water-splitting reaction apparatus.
NOVELTY - The stability improvement method involves performing photoelectrochemical reaction using n-type semiconductor containing metallic element e.g. vanadium and oxygen. Reaction solution is produced by dissolving metallic-element ion as the constituent element of semiconductor. The valence of metallic-element ion in reaction solution is pentavalence in steady state of reaction.    USE - Stability improvement method of visible-light responsible semiconductor photoelectrode for water-splitting reaction apparatus (claimed).    ADVANTAGE - Stability of semiconductor material in photoreaction is improved without using sacrificial reducing agent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a water-splitting reaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the apparatus used when light absorption inhibition occurred with the electrolyte solution. (Drawing includes non-English language text).
NOVELTY - Digestion purification tower is right hexagonal prism-shaped and is also designed to form cone-shaped structure by connecting to a column body, platform or other geometrical body. A main tower, purifying tower, separating tower, and sedimentation tank are also provided. Methane gas flows through reaction tower and releases through a hole. A liquid is also discharged from sedimentation tank water outlet.    USE - Digestion purification tower used for purifying biogas.    ADVANTAGE - The digestion purification tower enables to remove impurities during methane gas production in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a digestion purification tower.
NOVELTY - A waste oil or hogwash biodiesel is prepared by (a) performing esterification reaction with tetrabutyl titanate catalyst, (b) performing non-acid-ester exchange reaction, (c) dealcoholization, and simple distillation.    USE - Preparation of waste oil or hogwash biodiesel (claimed).    ADVANTAGE - Preparation process is efficient and environmentally friendly, and has fewer side effects and high yield. Product has good quality in asphalt, good weather resistance, low condensation point than conventional sulfuric acid, light color, and excellent quality, and does not erode device.
NOVELTY - An ammonia decomposing system comprises a windmill output power supply (10) provided with water and is used for converting wind energy into electric energy, shell(s) at least partially disposed in water, an electric power source connected to windmill, a water inlet pipe, and a water electrolysis device.    USE - An ammonia decomposing system for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an ammonia decomposing system.    Windmill output power supply (10)    Wind wheel shaft (11)    Tower frame (12)    Blade (14)    Knife handle (15)
NOVELTY - Catalyst comprising active components including calcium oxide and compound oxide, is new.    USE - The catalyst is useful for synthesizing biodiesel (claimed).    DETAILED DESCRIPTION - Catalyst comprising active components including calcium oxide and compound oxide of formula (M-Al-O), is new, where the ratio of the active components is 0.06-0.12 and M is magnesium or zinc. An INDEPENDENT CLAIM is included for preparation of catalyst.
NOVELTY - Preparing a saturated hydrocarbon, comprises heating an oligosaccharide to form a depolymerized oligosaccharide mixture, combining the depolymerized oligosaccharide mixture with a dicarbonyl under suitable conditions to form an intermediate mixture, and adding hydrogen and a hydrogenation catalyst to the intermediate mixture under suitable conditions.    USE - The process is useful for preparing a saturated hydrocarbon, such as 3-ethylnonane (all claimed), which is useful as fuels.    ADVANTAGE - The single pot process is provides saturated hydrocarbon with high quality.
NOVELTY - An anti-hair loss shampoo comprises non-ionic surfactant as decontamination foaming agent, foam stabilizing agent, thickening agent, emollient, chelating agent, pearlescent agent, preservatives, essence and pigment, olive oil and ginseng powder.    USE - Anti-hair loss shampoo (claimed).    ADVANTAGE - The anti-hair loss shampoo is economical and has excellent antibacterial effect. The anti-hair loss shampoo is manufactured by simple process with reduced consumption of energy.
NOVELTY - Separating and purifying high purity 3,2'',6''-tri-N-acetyl gentamicin C1a, comprises (a) diluting cobalt-removing solution, and separating impurities using a continuous chromatography column to obtain 3,2'',6''-tri-N-acetyl gentamicin C1a, (b) filtering an analyzing liquid using a nano-filtration membrane filter and concentrating the obtained filtrate, (c) conveying the obtained concentrated solution through a vacuum film by steam heating and concentrating, and (d) drying the concentrated solution by spray drying to obtain high purity 3,2'',6''-tri-N-acetyl gentamicin C1a.    USE - The method is useful for separating and purifying high purity 3,2'',6''-tri-N-acetyl gentamicin C1a (claimed).    ADVANTAGE - The method has high yield, and is economical, environmentally friendly and suitable for industrial production.    DETAILED DESCRIPTION - Separating and purifying high purity 3,2'',6''-tri-N-acetyl gentamicin C1a, comprises (a) diluting cobalt-removing solution, and separating impurities using a continuous chromatography column to obtain 3,2'',6''-tri-N-acetyl gentamicin C1a, where the cobalt-removing solution is diluted with aqueous ammonia until the P1 concentration is controlled to 1-9%, (b) filtering an analyzing liquid using a nano-filtration membrane filter with an interception relative molecular weight of less than 400, where the operation pressure is 0.12-0.35 MPa and the operation temperature is 5-40 degrees C, and concentrating the obtained filtrate until the mass concentration of 3,2'',6''-tri-N-acetyl gentamicin C1a reaches 5-15%, (c) conveying the obtained concentrated solution through a vacuum film by steam heating under the vacuum degree of 0.02-0.15 MPa and the operation temperature of 35-70 degrees C, and concentrating until the mass concentration of 3,2'',6''-tri-N-acetyl gentamicin C1a reaches 15-35%, and (d) drying the concentrated solution by spray drying to obtain high-purity 3,2'',6''-tri-N-acetyl gentamicin C1a.
NOVELTY - A biogas purification system comprises compressor connected inlet port and main components (a) and (b), vents, and polymer separation membrane which separates methane gas and carbon dioxide. The polymer separation membrane includes membrane (a) which delivers biogas from compressor, membrane (b) which discharges carbon dioxide delivered from membrane (a) to atmosphere, and separates methane gas contained in carbon dioxide, and membrane (c) which delivers methane gas discharged from membrane (a) to the collecting portion and separates carbon dioxide contained in methane gas.    USE - System is used for purifying biogas (claimed).    DETAILED DESCRIPTION - A biogas purification system comprises compressor connected inlet port and main components (a) and (b), vents, and polymer separation membrane which separates methane gas and carbon dioxide. The polymer separation membrane includes membrane (a) which delivers biogas compacted from compressor, separates biogas from methane gas and carbon dioxide, and discharges along both directions, membrane (b) which discharges carbon dioxide delivered from membrane (a) to the atmosphere, and separates methane gas contained in carbon dioxide, and membrane (c) which delivers methane gas discharged from membrane (a) to the collecting portion and separates carbon dioxide contained in methane gas.
NOVELTY - A crawler-type roller sludge turner comprises machine frame (V), rubber track undercarriage (IV), hydraulic system (II), turning roller (I), cooling system (III), automatic operation control device (VI), frame longitudinal beam (7), frame beam, reinforcing truss, fixed support, automatic control device, roller rocker arm, refrigerator (2), hydraulic controller (6) and telescopic oil cylinder (4).    USE - Crawler-type roller sludge turner for processing municipal sludge.    ADVANTAGE - The sludge turner has compact structure, small power consumption, high production efficiency, and good quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of crawler-type roller sludge turner.    Refrigerator (2)    Telescopic oil cylinder (4)    Hydraulic controller (6)    Frame longitudinal beam (7)    Turning roller (I)    Hydraulic system (II)    Cooling system (III)    Rubber track undercarriage (IV)    Machine frame (V)    Automatic operation control device (VI)
NOVELTY - Manufacture of nutritious soil comprises selecting 1 m3 straw, cutting into length of straw of 10-13 cm using knife, taking 50-60 kg soil from Bacillus subtilis or stack, soil crushing to less than 2 cm, uniformly mixing, piling, spraying 100-120 kg water to small stack, fermenting for 30-40 days, removing plastic film, fermenting, crushing 0.1-1 cm, adding 5-6 kg nitrogenous fertilizer, 4-5 kg potash fertilizer, 2-3 kg phosphate fertilizer, stirring uniformly, spraying 40-50 kg water, spreading and paving on road surface, drying, and packing into 2 kg bags.    USE - Method for manufacturing of nutritious soil (claimed).    DETAILED DESCRIPTION - Manufacture of nutritious soil comprises selecting 1 m3 straw, cutting into length of straw of 10-13 cm using knife, taking 50-60 kg soil from Bacillus subtilis or stack , soil crushing to less than 2 cm, uniformly mixing with straw small sections, piling steamed bread shape less, spraying 100-120 kg water to small stack, covering layer of plastic film, fermenting for 30-40 days, removing plastic film, fermenting straw into crusher, crushing 0.1-1 cm, adding 5-6 kg nitrogenous fertilizer, 4-5 kg potash fertilizer, 2-3 kg phosphate fertilizer, stirring uniformly, spraying 40-50 kg water, spreading and paving on road surface, drying, and packing into 2 kg bags.
NOVELTY - A mushroom cultivation material comprises 35-45 wt.% tea seed meal, 15-25 wt.% tea dust, 15-25 wt.% bagasse, 10 wt.% rice bran, 7 wt.% corn powder, 2 wt.% gypsum powder, and 1 wt.% lime powder.    USE - Mushroom cultivation material.    ADVANTAGE - The cultivation material has improved air-permeability and water-holding capacity, accelerates mushroom mycelium growth, shortens production period, increases mushroom production by 25-35%, widens channels for raw material cultivation, reduces production costs, and is very suitable for tea growing areas.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of cultivation material by exposing raw materials to sun for 1-2 days to kill bacteria by UV light; uniformly mixing tea seed meal and fresh tea dust, and mixing with 1% lime aqueous solution to obtain wet material; stacking wet material into heap with height of 1-1.2 m, width of 2-3 m and dry weight of 300-500 kg, inserting 10-15 cm wood sticks through the heap to form vertical holes with density of 1 unit/m3, and covering with straw mat and naturally fermenting; when material temperature reaches 60 degrees C, maintaining for 24 hours and turning once everyday, adding bagasse, rice bran, corn powder, gypsum powder and additives after turning for third time, adding water depending on water content of heaps, turning 4-5 times for 6-7 days auxiliary material, and stopping fermentation to obtain material with water content of 63-65%; packing the material in polypropylene bags at 1100-1200 g/bag, and sealing; and sterilizing under atmospheric pressure, holding for 8-10 hours when pot temperature reaches 100 degrees C, and naturally cooling to less than or equal to 25 degrees C; and    (2) application of cultivation material including inoculating strain into cultivation material, culturing in the dark at 22-24 degrees C and 60-75% relative humidity for 23-25 days, and performing fruiting management..
NOVELTY - Composting of vegetable waste comprises crushing vegetable waste into 6-8 cm length, adjusting water content to 50-60% and pH value to 7-9, placing in conical-shaped container, spreading with 15-20 cm rapeseed, covering 13-15 cm stack surface with dry soil and plastic film, reducing temperature to not greater than 40 degrees C, mixing, composting and maintaining temperature at 50-60 degrees C for 16-20 days.    USE - Method for composting vegetable waste (claimed).
NOVELTY - Blended fertilizer comprises biological microbial inoculum fertilizer bag with polypropylene packing bag containing 14.125-27.125 pts. wt. urea, 15.75-26.825 pts. wt. poly-sulfur coated urea, 24.133-24.728 pts. wt. diammonium phosphate, and 17.5-18.5 pts. wt. potassium chloride, and organic fertilizer comprising 2.397-8.926 pts. wt. biological microbial inoculum, 7.5-12.5 pts. wt. nitrogen, 22-26% phosphorus pentoxide, and 12-13% potassium chloride.    USE - Blended fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of blended fertilizer comprising adding urea, poly-sulfur coated urea, diammonium phosphate, potassium chloride and organic fertilizer in fertilizer bag, mechanically mixing uniformly, adding biological microbial inoculum, and packing into primary-secondary bag.
NOVELTY - A biodiesel plasticizer is prepared by mixing biodiesel, 1-20 wt.% small molecule carboxylic acid based on weight of biodiesel, and 1-10 wt.% titanium silicalite zeolite-based catalyst based on weight of biodiesel, slowly adding 10-30 wt.% hydrogen peroxide based on weight of biodiesel while stirring, and reacting at 40-80 degrees C for 3-6 hours.    USE - Production of biodiesel plasticizer (claimed).    ADVANTAGE - Production process is environment-friendly, has short reaction time, high reaction efficiency, and less side reaction, and eliminates use of sulfuric acid, emulsifier, or solvent, and product is environment-friendly, has high selectivity, high quality, and excellent color and luster properties.
NOVELTY - A bioorganic fertilizer comprises peat, urea, ammonium sulfate, potassium metaphosphate, potassium pyrophosphate, magnesium phosphate, chitin, phosphoric acid, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, Verticillium powder, Bacillus thuringiensis powder, Aschersonia powder, caterpillar fungus powder, cortex fraxini, and radix stemonae.    USE - Bioorganic fertilizer used for improving agricultural soil (claimed).    ADVANTAGE - The fertilizer has good water absorption and water retention, and nutrients required for plant growth, can improve soil physical properties and restore soil fertility.    DETAILED DESCRIPTION - A bioorganic fertilizer comprises 20-35 pts. wt. peat, 15-20 pts. wt. urea, 12-15 pts. wt. ammonium sulfate, 5-9 pts. wt. potassium metaphosphate, 1-3 pts. wt. potassium pyrophosphate, 4-8 pts. wt. magnesium phosphate, 0.5-1.5 pts. wt. chitin, 1-3 pts. wt. phosphoric acid, 5-9 pts. wt. potassium dihydrogen phosphate, 4-7 pts. wt. dipotassium hydrogen phosphate, 8-12 pts. wt. Verticillium powder, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 0.1-0.2 pts. wt. Aschersonia powder, 0.3-0.5 pts. wt. caterpillar fungus powder, 1-3 pts. wt. cortex fraxini, and 1-2 pts. wt. radix stemonae.
NOVELTY - This utility model claims a method for producing and distributing system technology field, especially relates to a kind of novel methanol gasoline preparation system, the utility model is a novel methanol gasoline distributing system, device and at the same time capable of fully mixing methanol and gasoline, effectively prevent explosion, and it further comprises, the bottom of the mixing tank is vertically provided with a micro-pore pipe, micro-pore pipe is provided with a micro-pore, the micro-pore pipe is connected with air outlet of the machine is connected with the top of the methanol tank, gasoline tank and the mixing tank are respectively provided with a first vent hole, the second vent hole and the third vent hole, a vent hole, the second vent hole and the third vent hole by an air pipe, and the first vent hole, the second vent hole and the third vent hole are provided with the top of the first filter device, a gasoline tank is provided with an exhaust pipe, the exhaust pipe is provided with a filter device and a one-way valve.
NOVELTY - This utility model claims a biomass forming fuel of high temperature dry distillation furnace, referring to a kind of biomass forming fuel furnace, comprising a furnace body is provided with a sealed inner cavity, wherein the furnace cavity is set in the furnace chamber, a furnace body inner cavity upper part of the dry distillation chamber. The upper part of the furnace body is provided with an inner furnace chamber is connected with several oxygen inlet, turned and connected with the furnace body, and the furnace body is provided with a humidity-discharging pipe, chamber of the humidity-discharging pipe and the furnace body are connected with each other. The high temperature carbonization furnace, a furnace chamber of the biomass of the dry distillation chamber carbonization dry distillation process, the heat energy utilization rate. This utility model of the carbonizing time is shortened from 1 days to 10 days, saves the biomass carbonizing a desired fuel. The lower furnace is natural environment outside the furnace, which greatly reduces the labour intensity of the worker, improves the working environment, improves the single furnace yield and product quality, and furnace body service life is greatly prolonged.
NOVELTY - This utility model claims a gasification furnace raw material capable of completely reacting the biomass gasification furnace, comprising a furnace body (5) is set on the furnace body (5) of the side part (1) set on the furnace body (5). the lower part of the furnace body (5), the upper part is provided with at least one air outlet (1) is connected with the air outlet pipe (4), pipe (4) is provided with a guide hole (9). The utility model has simple structure, convenient use, the raw material reaction completely, which greatly improves the utilization rate of the raw material.
NOVELTY - This utility model claims a kind of biomass carbonization gas recycling device, wherein it is mainly composed of is provided with smoke inlet tube (washing tower (1) with handle (2), a guide tube (3) is connected with the washing tower (1) is connected with the purifier (4), further is provided with an exhaust pipe on the cleaner (4) (5). This utility model not only has simple structure, but also has low cost, and also can process the biomass carbonization gas generated can be directly used for combustion of the pure gas, so as to change waste into valuable, so it is suitable to popularize and use.
NOVELTY - This utility model claims a kind of gas phase by using waste grease alcohol solution for esterification tower of biological diesel oil, esterifying tower comprising a cylinder body, a sealing head and a calotte, a sealing head is fixedly mounted on the bottom of the cylinder, a sealing head around a cylinder at the bottom of the calotte, the lower part is set with connecting pipe is a connecting pipe and methanol steam gas inlet, the bottom of cylinder is set with a discharging port, the upper part of the cylinder body is equipped with a discharging port. By the utility model is capable of using gas phase alcohol solution for producing biological diesel oil, so as to eliminate the acid-base waste water pollution, reduces device corrosion, does not need catalyst at an appropriate temperature and pressure, a manufacturing technique of a kind of green and environment-friendly, at the same time, it reduces the production cost. Use of the utility model is a gas phase alcohol craft with low investment cost, suitable conditions, at the same time, high yield, simple operation, it basically realizes automatic control, a totally-enclosed operation, basically no waste gas, waste water, the quality of the product is stable and reliable.
NOVELTY - The device has a battery stack module and a fuel cell stack module fixed on a fixing base. A heating device is connected with an outer part of the fuel cell stack module. A pressurizing device is provided with a pressurizing column that is connected with an upper part of the fuel cell stack module. A pressure support device is provided with a top plate and two upright posts that are connected with the heating device. An end of the heating device is fixed on the fixing base and another end is fixed on the top plate.    USE - Solid oxide fuel cell stack manufacturing and testing device.    ADVANTAGE - The device avoids battery cell stack cornering problem in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a solid oxide fuel cell stack manufacturing and testing device.
NOVELTY - A core-shell structure hollow microsphere comprises tungsten trioxide as core and porous silica as shell, and has diameter of 500-600 nm.    USE - Core-shell structure hollow microsphere used as catalyst for esterification of biodiesel (claimed).    ADVANTAGE - The microsphere has good catalytic effect and high esterification rate of up to 97.6%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) included for preparation of microsphere by (A) putting 100 ml anhydrous ethanol in beaker, adding 0.44 g cetyltrimethylammonium bromide (CTAB), stirring to dissolve to obtain CTAB solution; putting 50 ml ethanol in another beaker, adding 1.15 g phosphotungstate, stirring with glass rod to dissolve, dropping CTAB solution, continuously stirring for 30 minutes, reacting, filtering to obtain hexadecyltrimethylammonium phosphotungstate, and drying; (B) mixing 70-200 mg hexadecyltrimethylammonium phosphotungstate and 110 mg CTAB in round bottom flask, adding 20 ml anhydrous ethanol, dispersing in ultrasonic bath for 30 minutes to obtain solid, mixing with 30-80 ml distilled water at 28 degrees C while stirring for 6 hours, adding 0.3 ml ammonia and 0.4-0.6 ml tetraethyl orthosilicate, continuously stirring for 16 hours, filtering, and drying to obtain microsphere; and (C) roasting in muffle furnace at 450 degrees C and at 1 degrees C/minute for 4.5 hours; and    (2) esterification of biodiesel by esterifying oleic acid and methanol at mass ratio of 1:5-2 at 90 degrees C for 8 hours in the presence of core-shell structure hollow microsphere as catalyst.
NOVELTY - The furnace has a furnace body (1) provided with a feeding device (2) that is fixed with a feed port (11). A top part of the furnace body is fixed with a gas outlet (12). An ash falling device (4) is mounted on the furnace body. The feeding device is connected with an opening that is formed at a bottom part of a hopper. A feeding sliding seat is connected with a blanking seat that is provided with a feeding channel and a feed hopper. A combustion supporting device (3) and the furnace body are connected with a machine frame (10).    USE - Biomass furnace.    ADVANTAGE - The furnace prevents consumption of more fuel and improves fuel utilization rate, and has better energy-saving effect, and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass furnace.    Furnace body (1)    Feeding device (2)    Combustion supporting device (3)    Ash falling device (4)    Machine frame (10)    Feed port (11)    Gas outlet (12)    Feeding channel (221)
NOVELTY - The method involves igniting liquid hydrogen-oxygen fuel in a reaction furnace, and gasifying liquid hydrogen-oxygen fuel in the reaction furnace. Liquid hydrogen-oxygen fuel combustion is performed to generate fuel gas and carbon particles. Temperature of the reaction furnace is monitored in real-time. The temperature in the reaction furnace is controlled by adjusting amount of a combustion improver. The generated fuel gas and carbon particles are collected.    USE - Method for preparing biomass fuel by using solid organic waste.    ADVANTAGE - The method enables improving fuel utilization rate, ensuring energy-saving and environment-friendly effect and discharging fuel while stirring carbon particles to prevent stacking of the fuel in the furnace during burning process so as to ensure stable and long working time and prevent fuel particle generating slag at high temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for preparing biomass fuel by using solid organic waste.'(Drawing includes non-English language text)'
NOVELTY - The device has a stirring head (45) sleeved on a rotating shaft (43). A stirring motor (46) is fixed on a mortar unit (44). A lower end of the rotating shaft is extended out of the mortar unit. An output end of a chain wheel transmission mechanism (48) is connected with the rotating shaft. An impeller (47) is sleeved on the rotating shaft that is sleeved with a strip-shaped structure ash disk (42). Multiple ash falling areas are uniformly distributed along a circumferential direction. The ash disk is arranged on an upper end face of an ash-retention part.    USE - Biomass reaction furnace stirring and ash falling device.    ADVANTAGE - The device can accelerate material into ash with high rate, and effectively solves slag production problem from raw material particles during high temperature and alternately carries out dust and gas blocking actions. The device prevents mutual influence between furnace ash barrels during combustion process so as to provide better dust effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass reaction furnace stirring and ash falling device.    Strip-shaped structure ash disk (42)    Rotating shaft (43)    Mortar unit (44)    Stirring head (45)    Stirring motor (46)    Impeller (47)    Chain wheel transmission mechanism (48)
NOVELTY - The generator has a first container whose upper end is provided with a cooling water inlet and a feeding port and lower end is provided with a circulating water pipe and a carbon outlet. An outlet of a fuel gas output pipe is connected at a lower part of the first container, where inner surface of the first container is provided with a burning head and a combustion head. A constant-pressure closed container is fixed at an upper end of a second container that is provided with the cooling water inlet and a carbon inlet. The carbon outlet is fixed with the carbon inlet through a conveyor.    USE - Biomass gas reaction generator.    ADVANTAGE - The generator improves heat value of the biomass fuel in an effective manner, reduces discharging of the wastage gas and wastage residue and provides better cleaning process, and has better energy saving effect and high efficiency, and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas reaction generator.
NOVELTY - A fuel comprises 80-90 wt.% methanol, 2-5 wt.% additive, and 10-15 wt.% solvent oil. The additive comprises 25-30 wt.% tribetol, 20-30 wt.% petroleum ether, 5-10 wt.% acetone, 10-15 wt.% isobutyl alcohol, 5-10 wt.% nitromethane, 2-4 wt.% ethyl acetate, 4-8 wt.% plant oleic acid, 0.02-0.05 wt.% benzotriazole, 1-3 wt.% barium petroleum sulfonate, and 0.02-0.04 wt.% Sudan IV. The solvent oil is solvent oil number 120, solvent oil number 190, naphtha, or gasoline.    USE - Fuel used for car (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fuel comprising adding additive into synthesis tank, adding methanol, uniformly mixing, adding solvent oil, uniformly mixing, synthesizing, uniformly mixing, and standing for 30-60 minutes.
NOVELTY - Preparation of energy-saving fuel comprises mixing 20-80 wt.% ethanol and gasoline or diesel oil.    USE - Method for preparation of energy-saving fuel (claimed) used for vehicles, ships, aircraft, and other machinery or equipment.    ADVANTAGE - The fuel is saves energy and reduces emission.
NOVELTY - Preparation of fructus momordicae seed bio-oil comprises drying fructus momordicae seed, crushing to obtain powder, weighing, adding into high-pressure reaction kettle, adding water, sealing, preheating, reacting, cooling, collecting reaction mixture, extracting using organic solvent, separating and filtering to obtain organic phase, and distilling to remove organic solvent.    USE - Method for preparing fructus momordicae seed bio-oil (claimed).    ADVANTAGE - The economical method uses water as reaction solvent which is low-cost, non-toxic and harmless, thus reducing pollution and investment cost. The production of bio-oil from biomass solves the problem about energy crisis caused by depletion of petroleum resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of preparation of fructus momordicae seed bio-oil (Drawing includes non-English language text).
NOVELTY - The method involves fixing a glass tube with a Y-shaped three-way pipe. A latex tube is fixed with the Y-shaped three-way pipe. A common funnel is connected with an electrolytic chamber. The Y-shaped three-way pipe is fixed with a panel. A music card is adhered on a display board. A sensitive current meter and the music card are connected with a buzzer and an LED in a series manner. Hydrogen (H2) and oxygen (O2) are stored in a U-shaped tube. An end of a branch pipe is connected with a connector. Energy conversion operation is performed to achieve experimental effect.    USE - Method for manufacturing a changing electrode material generating hydrogen-oxygen fuel cell teaching tool that is utilized during fuel cell demonstration experiment in a classroom.    ADVANTAGE - The method enables generating current and utilizing the LED, the music card, a small lamp bead and a small motor, thus enhancing user interest, persuasion performance and practical value of a teaching tool.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a changing electrode material generating hydrogen-oxygen fuel cell teaching tool.'(Drawing includes non-English language text)'
NOVELTY - The method involves receiving charging control instruction. The charging control instruction is contained with charging stopping control command. The charging stopping control command is generated according to preset power charging or discharging instruction under power grid load condition. Electric automobile charging and discharging power level is controlled according to the preset power charging or discharging instruction. Grid charging and discharging power level is controlled under charge/discharge condition. The charging control command is contained with discharge command.    USE - Intelligent method for controlling charging process of a fuel cell in an electric automobile (claimed).    ADVANTAGE - The method enables realizing intelligent electric automobile fuel cell charging controlling process in an effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an intelligent system for controlling charging process of a fuel cell in an electric automobile    (2) an electric automobile.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an intelligent method for controlling charging process of a fuel cell in an electric automobile.'(Drawing includes non-English language text)'
NOVELTY - This utility model claims a hydrogen fuel generator, comprising a reaction tank, a feeding port, an air supply assembly and a fuel input part. According to this utility model, which is the air into the reaction space of the reaction tank through the air supply assembly, and injecting liquid methyl alcohol from feeding port, water and catalyst to the reaction space, after which react with each other to form hydrogen molecules, and generating hydrogen fuel and the air, finally, a fuel input part is generated by the hydrogen, the said hydrogen generator and a furnace for cooking or heating. Therefore, the hydrogen fuel production using traditional electrolytic water, the utility model is a hydrogen fuel generator does not need to cost too much electric energy can also produce hydrogen fuel, it not only can effectively reduce the manufacturing cost, but also can improve the economic value and application.
NOVELTY - A livestock and poultry waste water resource utilization and processing device, comprising an anaerobic tank, a grid tank, an adjusting pool, an aeration biological filter tank (BAF), a disinfection tank, a sludge tank, a sludge dewatering device, a gas collecting device. This utility model is a new-type anaerobic digestion marsh gas producing technique, BAF technique, technology for livestock and poultry breeding waste water source, it is processed by anaerobic fermentation for producing biogas production waste water and marsh gas and separating solid from liquid, solid slag and producing organic fertilizer is used as raw material to produce organic fertilizer, waste water by recycling and discharging and BAF technique and sterilizing, the processing effect is good, the energy consumption is low, use of the resource at the same time is provided with economic benefit.
NOVELTY - This utility model claims a kind of heating continuous biomass carbonization device furnace body, the whole structure whose upper part is cylindrical and lower part is reverse conical, the upper part is provided with an air channel 13, an air passage 12 of air inlet passage and a port 4, a port 6, a port 7, a port in the hearth by the draught fan air keeping micro positive pressure environment. The furnace body is divided into 9 row is set with 36 air inlet 5 a, which not only can pass through a temperature probe is installed in the monitoring furnace through air inlet valve is set with the air inlet quantity in the furnace temperature. The top end of the furnace wall is provided with a water sealing groove (1), which can improve the sealing property of the device. Grate 8 and door 9 is located in the lower part of the furnace body, which is mainly used for a. The hearth from the upper to the lower in turn a material preparing section, drying section, a pyrolysis section and a carbonization section, it can realize the continuous production bio-char; by adjusting the air inlet amount, capable of effectively controlling the furnace temperature, improves bio-char quality.
NOVELTY - This utility model claims a kind of heating continuous biomass carbonization device cylinder, mainly comprising a cylinder (1), a locating rod (2) and bracket (3), the upper part of the outline is semi-spherical, the lower part is cylindrical, the bottom opening, the cylinder thickness of 2.5 to 3 mm nm. Drying cylinder the lower part a 4 of bracket 3, bracket 3 can be directly installed in the tapered hole of the furnace body, there is no need to be fixed. The middle upper part of the drying cylinder is provided with 4 locating rod (2), a locating rod for locating the drying cylinder, drying cylinder assembly and disassembly by adjusting the length of the locating rod, it is convenient to operate. Drying the furnace tube in the body biomass raw material is divided into thin layer, a thin-layer counter-current hot air drying principle, it can accelerate drying of the material, which is good for improving a production efficiency and improve bio-char quality.
NOVELTY - This utility model claims a kind of biological diesel oil with low acid value of production equipment, comprising an adsorption column, a high-level tank, methanol tank, receiving groove and pipeline, the adsorption column is filled with D301-FC non-polar macro-porous adsorption resin, the biological diesel oil tank and a methanol tank connected with the inlet of the adsorption column, the receiving groove is connected with the outlet of the adsorption column. This utility model adopts D301-FC non-polar macroporous absorption resin to absorb the acidic substance, the acid value is reduced to less than 0.6, simple equipment, convenient operation, low operation cost, and it is suitable for mass continuous operation.
NOVELTY - This utility model claims a biogas purifying system, solves the problem that the existing system in a high investment cost, high operation cost, high failure rate and purifying purity is low. A connected according to the order of the anaerobic tank (1), a particle filter (2), a drying tower (3), a desulfurizing tower (4), gas holder (5), a steam-water separator (6), a low pressure marsh gas compressor (7), the formula (8), a freezing type drying machine (9), a coalescing type filter (10), an oil-water separating filter (11), a precise filter (12) is, a heater (13), a CO2/CH4 high efficiency separating film (14), a CO2/CH4 film (19) and the marsh gas storage tank (20), a first CO2/CH4 efficient separation membrane (14) rich gas outlet (15) and the carbon dioxide purifying device (16) is connected with a carbon dioxide storage tank in a carbon dioxide purifying device (16) (17). This utility model can make the raw material gas of the carbon dioxide removing, purifying rate is high.
NOVELTY - This utility model claims a pumping type multi-parameter measuring device, wherein the measuring device comprises a micro-air pump and PIC16F886 single chip microcomputer, an air outlet end of the micro-air pump is connected with the methane probe, an oxygen probe, a carbon monoxide probe and hydrogen sulphide probe, methane probe, an oxygen probe, a carbon monoxide probe, a hydrogen sulphide probe is connected with the single chip, a first voltage stabilizer and the display is connected with the single chip, the second voltage stabilizer is connected with the methane probe, a third voltage stabilizer and the oxygen probe, a carbon monoxide probe, a hydrogen sulphide probe, the fourth voltage stabilizer is connected with the voltage stabilizer with carbon monoxide probe, a hydrogen sulphide probe, the single chip and the display, a buzzer, a key. A test environment, removing oxygen in real time, a concentration of carbon monoxide, hydrogen sulphide, and date, clock, week, a voltage display, capable of detecting the environment gas concentration value a m. Used for underground coal mine methane detecting member a portable carrying for alarming.
NOVELTY - The system (100) has an elevated water reservoir (102) that is positioned at a predetermined altitude to store water. A ground water reservoir (106) is positioned at ground level to receive water separated from turbine (104) through water outlet channel. An electrolysis chamber (108) is connected to reservoir for receiving water to separate oxygen and hydrogen from the received water. A fuel cell (110) is provided for combining both oxygen and hydrogen to form water and transfer the water to elevated water reservoir through the outlet connected between fuel cell and reservoir (102).    USE - System for recycling hydro power production.    ADVANTAGE - The oxygen collecting chamber is used to collect the oxygen from the environment to form the water by combining the oxygen and hydrogen. The carbon foot print in the power production can be reduced. The water is recycled to obtain more hydro power than power used to split water into hydrogen and oxygen. The clean power can be produced by combining the fuel cells and hydro power from higher altitudes. The power from higher altitude can be generated with limited power resources. The clean power can be generated without disturbing the environment by adapting recycling hydro power production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for recycling hydro power production.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for recycling hydro power production.    System for recycling hydro power production (100)    Elevated water reservoir (102)    Turbine (104)    Ground water reservoir (106)    Electrolysis chamber (108)    Fuel cell (110)
NOVELTY - Coal and biomass are pulverized separately, to obtain powdered coal and biomass powder. The biomass powder is dry-distilled, to obtain dry-distilled biomass, dry distillation gas and tar. The dry-distilled biomass and powdered coal are spin-dehydrated by heating. The obtained mixture is mixed with the tar for covering mixture using tar, to obtain solid fuel. The combustion heat formed while pulverizing biomass is used for spin-dehydration process.    USE - Manufacture of solid fuel used for power generation.    ADVANTAGE - The method enables manufacture of solid fuel with high efficiency safely.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (11) for manufacturing solid fuel, which has a dry distillation apparatus (17) for dry-distilling the biomass, a separator (19) inducing the dry-distilled product discharged from the dry distillation apparatus, and isolating dry-distilled gas and tar, a mixer (21) mixing the dry-distilled biomass and powdered coal for obtaining mixture, a mixer (25) mixing spin-dehydrated mixture from a dehydrator (23), and tar obtained from separation apparatus, a combustion apparatus (27) generating combustion exhausting gas used as heat source for dehydrator, and a circulation piping (29) circulating thermal medium between the dehydrator and combustion apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for manufacturing solid fuel. (Drawing includes non-English language text)    Apparatus (11)    Dry distillation apparatus (17)    Separator (19)    Mixers (21,25)    Dehydrator (23)    Combustion apparatus (27)    Circulation piping (29)
NOVELTY - Method for reducing ash content of agropellets, involves mixing agricultural by-product powder and wood powder in weight ratio of 50-70:30-50.    USE - Method for reducing ash content of agropellets (claimed).
NOVELTY - Method for producing isobutanol, involves growing recombinant yeast host cell which produces isobutanol and comprises mitochondria substantially devoid of threonine deaminase activity, where the recombinant yeast cell is grown under conditions where isobutanol is produced.    USE - The method is useful for producing isobutanol using yeast chosen from Saccharomyces, Schizosaccharomyces, Hansenula, Candida, Kluyveromyces, Yarrowia and Pichia (all claimed), where the isobutanol is useful as industrial chemical, fuel additive, feedstock chemical in plastic industry, and food grade extractant in food and flavor industry.    ADVANTAGE - The method provides high yield of isobutanol without using intermediates.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recombinant yeast host cell capable of producing isobutanol, comprising mitochondria substantially devoid of threonine deaminase activity, pyruvate dehydrogenase activity, and isopropylmalate synthase activity.
NOVELTY - A method for making fuel, involves converting biomass from a culture primarily comprising a C1 metabolizing non-photosynthetic microorganism into an oil composition and refining the oil composition into a fuel.    USE - For making fuel, where the fuel comprises jet fuel, diesel fuel, paraffinic kerosene, and/or gasoline (claimed); and for making biofuels, bioplastics, or the like.    ADVANTAGE - The composition has an octane number of 85-120 or an octane number greater than 90. The method provides improved method of efficiently and cost-effectively producing alternative fuels without taxing the environment or competing with food production. The method solves the problem of prior art by providing efficient and cost-effective methods for producing biofuels and other products using bioengineering. The method effectively uses methylotroph or methanotroph bacteria as a new host system to generate biomass for biofuel in the form of e.g. esterified biodiesel or alkane fuels for hydrotreatment, or for bioplastics in form of polyhydroalkanoates (PHAs).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biofuel composition comprising molecules containing hydrogen and carbon atoms, where the hydrogen and carbon atoms are at least 80 wt.% of the weight of the composition and the delta 13C distribution of the composition is less than about -37%.
NOVELTY - An isolated microbial culture for converting lignocellulosic biomass to a biofuel and/or another carbon-based chemical comprises a first microorganism belonging to the genus Caldicellulosiruptor and a second microorganism belonging to the genus Thermoanaerobacter.    USE - For converting lignocellulosic biomass to a biofuel and/or another carbon-based chemical (claimed).    ADVANTAGE - The method provides numerous microbiological co-cultures for increasing the efficiency of ethanol and/or lactic acid production from biomass. The combination of microorganisms in the production methods offers benefits relating to: a) high growing and process temperatures, resulting e.g. in a lower contamination risk in the production process and e.g. ethanol as a production product can be simultaneously distilled during the fermentation process; b) high ethanol tolerance (tolerance of approximately 4% ethanol); c) high inhibitor tolerance; d) broad substrate specificity, and capable of utilizing pentoses such as xylose and arabinose and of hexoses such as glucose, mannose, fructose and galactose as well as cellulose and xylan; e) improved ratio of ethanol:lactate:actetate. The combination of the two different microorganisms that co-culture these microorganisms are able to convert highly complex poylsaccharides like cellulose and/or xylan with higher efficiency and better yields of carbon based chemicals like ethanol and/or lactic acid than either microorganism alone.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for converting lignocellulosic biomass to a biofuel and/or another carbon-based product, involving: contacting the lignocellulosic biomass with a microbial co-culture for a period of time at an initial temperature and initial pH, thereby producing an amount of a biofuel and/or other carbon-based chemicals.
NOVELTY - Method for producing methane, involves contacting methanogenic microorganisms in a reaction vessel with hydrogen and carbon dioxide, where the gas feed rate of hydrogen and carbon dioxide into the reaction vessel is at least 1 volume per volume per minute (vvm) in total or at least 1.2 wm in total.    USE - The method or system is useful for producing methane (all claimed).    ADVANTAGE - The method consumes carbon dioxide and reduces the amount of the greenhouse gases in the atmosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for producing methane which comprises at least one device for generating electric energy from a renewable and/or nonrenewable energy source, at least one device for producing hydrogen and/or oxygen by the electrolysis of water and/or brine, and at least one bioreactor comprising a reaction vessel suitable for growing, fermenting and/or culturing methanogenic microorganisms and at least one device for providing a gas feed of hydrogen and carbon dioxide into the reaction vessel.
NOVELTY - Frictional dragging pyrolysis of biomass, comprises (i) adding biomass into closed frictional pyrolysis apparatus, extruding biomass in a screw extrusion unit, and then passing into rotor frictional dragging unit; (ii) rotating the biomass in the rotor frictional dragging unit, and carrying out frictional pyrolysis of the biomass to obtain mixed product; (iii) allowing the mixed product to settle, and separating the charcoal powder and solid product; and (iv) carrying out gas-liquid separation of the remaining mixed product to obtain crude gas and water-oil liquid.    USE - The method is useful for frictional dragging pyrolysis of biomass (claimed).    ADVANTAGE - The method is simple to operate, realizes zero residual and zero discharge, and is environmentally friendly.
NOVELTY - Dual phase catalyst system comprising a water soluble acid catalyst that is soluble in water, and a solid acid catalyst that is insoluble in water, is new, where the catalyst system is capable of hydrating the mixed olefins without requiring separation of the mixed olefins prior to contacting with the dual phase catalyst system, and converting the mixed olefins into the mixed alcohols at a conversion rate that is greater than either the conversion rate of the water soluble acid catalyst or the conversion rate of the solid acid catalyst.    USE - The catalyst system is useful for producing mixed alcohols including butanols such as 2-butanol and tertiary-butanol from mixed olefins (all claimed), where the butanols are useful as useful fuel components, oxygenates, and octane enhancers.    ADVANTAGE - The inexpensive catalyst system allows for the direct catalytic hydration of alkenes to alcohols.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing mixed alcohols from mixed olefins using the catalyst system, comprising introducing the mixed olefins to the catalyst system such that the mixed olefins contact the catalyst system, maintaining the catalyst system such that the mixed olefins convert into the mixed alcohols, and removing the mixed alcohols from the catalyst system.
NOVELTY - Preparing dinoprostone (i.e. prostaglandin E2), comprises converting 11 hydroxyl group of prostaglandin PG F2 into 15 hydroxyl group, then performing oxidation to 9 hydroxyl to obtain ketone carbonyl, adding protecting group, and hydrolyzing to de-protect using hydrolysis system for reacting.    USE - The method is useful for preparing dinoprostone (claimed).    ADVANTAGE - The method prepares dinoprostone with high yield and high purity in a cost-effective, environment friendly, convenient, short production period.
NOVELTY - Preparation of xylometazoline hydrochloride comprises reacting m-xylene and tertiary butyl alcohol in the presence of Lewis acid, reacting with formaldehyde under the action of hydrochloric acid and a catalyst; reacting with sodium cyanide, mixing with ethylenediamine-toluene sulfonic acid salt, heating for cyclization, alkali precipitating p-toluene sulfonic acid xylometazoline; and reacting with hydrochloric acid to obtain the xylometazoline hydrochloride.    USE - Method for preparing xylometazoline hydrochloride (claimed).    ADVANTAGE - The method is simple, avoids using toxic and corrosive reagent, has mild reaction condition, less side reaction, easy post-treatment, and high product purity and yield, reduces labor intensity, and improves working environment.
NOVELTY - The system (10) has an energy source (17) arranged in a gasification plant. A feedstock supply delivers a solid feedstock. A feed bin is arranged downstream of the feedstock supply. The feed bin receives the solid feedstock and provides a dry feedstock. A gasifier (16) is arranged downstream of the feed bin. The gasifier produces syngas from the dry feedstock. A heating system uses the energy to heat the solid feedstock directly. The heating system heats the solid feedstock indirectly and removes moisture from the solid feedstock in the feed bin.    USE - System for preheating feedstock i.e. high moisture content feedstock such as low rank coals e.g. PRB coal and/or biomass.    ADVANTAGE - The system applies different energy sources to dry the feedstock in the feed bin, so that feedstock flowability is improved, thus improving overall plant efficiency. The system selects and combines energy sources that are unused, so that the efficiency of the plant is improved, thus realizing cost optimization. The system utilizes the energy source to provide dry fuel, so that the energy used for converting the feedstock to the syngas is reduced, thus providing increased flow of the dry fuel, and hence providing improved protection against frozen fuel and/or minimize abrasion-related issues.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for preheating feedstock.    System for preheating feedstock (10)    Fluidization system (11)    Drying system (13)    Gasifier (16)    Energy source (17)
NOVELTY - The system (1) has an off-gas hydrogen discharge line (L1) for connecting a solid oxide fuel cell (SOFC) (11) and first catalyst (13), where off-gas (G1) i.e. exhaust gas, is circulated from the SOFC for the catalyst at time of rated operation. A first communication discharge line (L4) circulates the off-gas such that an end part connects the first catalyst to circulate second catalyst (12). Heat exchangers (14, 15) are connected in a middle part of the first communication discharge line and a second communication discharge line (L5) to circulate the catalysts.    USE - Fuel cell system i.e. SOFC system, for generating electric power. Can also be used as a polymer electrolyte fuel cell (PEFC) system.    ADVANTAGE - The off-gas hydrogen discharge line connects the SOFC and the first catalyst such that the off gas is circulated from the fuel cell for the first catalyst at time of the rated operation, so that the system can suppress exhaustion of the catalyst that is used for combustion of off-gas hydrogen by burning the off-gas hydrogen reliably, thus carrying-out efficient heat exchange.    DETAILED DESCRIPTION - The off gas includes off-gas hydrogen and off-gas oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system at time of starting of a fuel cell.    Off-gas (G1)    Off-gas hydrogen discharge line (L1)    Communication discharge lines (L4, L5)    Fuel cell system (1)    SOFC (11)    Catalysts (12, 13)    Heat exchangers (14, 15)
NOVELTY - Composite wood product comprises 0.5-6 wt.% of lignosulfonate, wood particles, and 1-10 wt.% of ground corn, where the wood product has a moisture content of 1-10 wt.%, and is free of wax.    USE - The composite wood product is useful for burning (claimed), grilling, heating, and building fires, in fireplaces, woodstoves, outdoor fire pits, chimineas, and campfires, as a source of heat or ambience, in restaurants for brick ovens or grills, in campgrounds and state or federal parks for preventing the spread of insects or disease, and as a substitute for cordwood or wax based fire logs.    ADVANTAGE - The composite wood product: is easy to ignite and manipulate while burning; produces a pleasant aroma; generates sufficient heat and flames, over an extended period of time; burns and emits less carbon dioxide and other greenhouse gases; and is insect-free, easier to store, and burns more evenly without sparks.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the composite wood product adapted for burning, comprising providing the composite wood product, and burning the composite wood product to produce smoke comprising a lack of malodorous content.
NOVELTY - The apparatus comprises a reactor into which a surfactant solution is supplied, an on-off control valve, a solution storage tank, a metal pipe, a heating coil, and a conveyor belt.    USE - The apparatus is useful for producing gas hydrate such as hydrate former, semi-clathrate, tetrahydrofuran, 1,3-dioxolane, tetrahydropyran, cyclopentane, acetone, difluoromethane, isobutane, iso-butylene, n-butane, propane, liquefied pertoleum gas, methylcyclohexane, methylcyclopetane, neohexane, methyltertbutyl ether, adamantine, tetra-n-butylammonium bromide, tetra-n-butylammonium fluoride and tetra-n-butylammonium chloride (all claimed).    ADVANTAGE - The apparatus enables continuous production of gas hydrate in an economical manner, and has improved durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing hydrate gas.
NOVELTY - Use of a gaseous mixture consisting of propane in a concentration of 71-79 wt.% and a gas consisting of isobutene and/or butene in a concentration of 21-29 wt.% as a replacement or alternative refrigerant gas for 1,1,1,2-tetrafluoroethane (R134a) and/or for other refrigerants, which are replacements or alternatives to R134a containing hydrofluorocarbons (HFC), hydrofluoroolefins (HFO) and hydrofluoro ethers (HFE), is claimed.    USE - The gaseous mixture is useful: as a replacement or alternative refrigerant gas for R134a and/or for other refrigerants, which are replacements or alternatives to R134a containing HFC, HFO and HFE; in air-conditioning or refrigeration plants; and as a refrigerant in air-conditioning systems of motor vehicles, refrigerated cabinets for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air-conditioning plants, domestic, commercial and industrial chillers, air-conditioning or refrigeration plants in the process industry, refrigerated transport, chilled water dispensers, commercial ice machines, and domestic, commercial and industrial dehumidifiers (all claimed).    ADVANTAGE - The gaseous mixture can be made using low-cost raw materials, thus inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for retrofitting process in existing air-conditioning or refrigeration installations, comprising replacing the refrigerant gas used in the plant with the gaseous mixture.
NOVELTY - Use of a gaseous mixture selected from: 85-95 wt.% dimethyl ether and 5-15 wt.% propylene, and 71-85 wt.% dimethyl ether and 15-29 wt.% propane, is claimed as a replacement or alternative refrigerant for 1,1,1,2-tetrafluoroethane (R134a) and/or for other refrigerants which are replacements or alternatives to R134a containing hydrofluorocarbons (HFC), hydrofluoro olefins (HFO) and hydrofluoro ethers (HFE).    USE - The gaseous mixture (dimethyl ether and propylene, and dimethyl ether and propane) is useful as a replacement or alternative refrigerant for R134a and/or for other refrigerants, and used in air-conditioning or refrigeration plants, and in air-conditioning systems of motor vehicles, refrigerated cabinets for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air- conditioning plants, domestic, commercial and industrial chillers, air-conditioning or refrigeration plants in the process industry, refrigerated transport, chilled water dispensers, commercial ice machines, and domestic, commercial and industrial dehumidifiers (all claimed).    ADVANTAGE - The gaseous mixture makes it possible to obtain thermodynamic characteristics that are particularly suitable and improved for replacing R134a.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) air-conditioning or refrigeration plant containing, as a refrigerant, the gaseous mixture; and    (2) retrofitting process in existing air-conditioning or refrigeration plants, comprising the replacement of the refrigerant gas used in the plant with the gaseous mixture.
NOVELTY - As replacement or alternative refrigerant gas for R404A, R507A and/or R407C, and/or other refrigerants, which are replacement or alternative refrigerants for R404A, R507A and R407C containing hydrofluorocarbons (HFC), hydrofluoroolefins (HFO) and hydrofluoroethers (HFE), a gaseous mixture comprising 90-99 wt.% propylene and 1-10 wt.% gas selected from butene, ethylene and/or ethane, is used.    USE - As replacement or alternative refrigerant gas for R404A, R507A and/or R407C, and/or other refrigerants; in air-conditioning or refrigeration plants; and in air-conditioning systems of motor vehicles, refrigerated cabinets for supermarkets, cold stores, domestic refrigerators, centrifugal chillers, domestic, commercial and industrial air- conditioning plants, domestic, commercial and industrial chillers, air-conditioning or refrigeration plants in the process industry, refrigerated transport, chilled water dispensers, commercial ice machines, and domestic, commercial and industrial dehumidifiers (claimed).    ADVANTAGE - The gaseous mixture have lower production cost and an improved environmental impact, particularly in terms of global warming potential, hence capable of satisfying environmental norms, even in long term.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) refrigerant gaseous mixture consisting of 93-97 wt.% propylene and 7-3 wt.% ethylene;    (2) refrigerant gaseous mixture consisting of 90-99 wt.% propylene and 1-10 wt.% butene;    (3) air-conditioning or refrigeration plant containing the gaseous mixture as a refrigerant; and    (4) retrofitting process in existing air-conditioning or refrigeration plants, involving replacement of the refrigerant gas used in the plant with gaseous mixture comprising 90-99 wt.% propylene and 1-10 wt.% gas selected from butene, ethylene, ethane and/or and propane.
NOVELTY - Method (M1) of consolidated bioprocessing for production of L(+)-lactic acid and/or lactate involves providing fermentation medium comprising carbon source, ammonium sulfate, yeast extract, magnesium chloride, calcium chloride, and trace metals; inoculating the medium with microbial culture which is gram positive thermophilic and cellulolytic bacterial isolate Paenibacillus macerans IIPSP3 (MTCC 5569); incubating the medium at 40-55 degrees C; and adding sterile neutralizing agent to the medium in 4-8 hours of incubation to maintain pH of the medium in the range of 5-7.2.    USE - For consolidated bio processing of lignocellulosic biomass to L(+)-lactic acid and/or lactate.    ADVANTAGE - The method provides one step production of L-Lactic Acid from low cost non edible feedstock lignocellulosic biomass by using thermophilic bacteria Paenibacillus macerans IIPSP3 (MTCC 5569), which is not only capable of hydrolyzing cellulose to glucose but also further fermenting it to L-Lactic Acid under aerobic conditions, without any growth inhibition in presence of lignirt. The method has less chances of contamination, as the fermentation is carried out at higher temperatures and is economically attractive, as preferably no external enzyme loadings are required. In the method no extra capital investment needs to be done as required in traditional methods such as separate hydrolysis and fermentation (SHF). The utility cost is also highly reduced in CBP process. Up-scaling of the method is easier as the method does not require stringent conditions of anaerobicity. As there is no or minimal requirement of enzyme from external sources, the operating cost of the method is reduced. Optically pure L(+) form of lactic acid is formed without any by-product contamination making downstream processing easier and cheaper.
NOVELTY - The system (100) consists of SOFC (120) and a SOEC (110) that are stacked together, respectively. The SOEC is equipped with a cathode (111) and an anode (113) that are connected with a cathode (121) and a anode (123) of a SOFC, by a fluid metal channel line (131,133) respectively. A pair of insulating layer (141,143) is formed on the respective metal channel lines. The cathode and anode of the SOEC flow the hydrogen and oxygen to the cathode and anode of the SOFC, and generate the electric power.    USE - Hybrid electric power generation system.    ADVANTAGE - The fuel cost of electric power generation system is reduced. Therefore, the electric power generation system is environment-friendly, and the productivity of the electric power is improved without using separate energy storage device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hybrid electric power generation system. (Drawing includes non-English language text)    Hybrid electric power generation system (100)    SOEC (110)    Cathode (111,121)    Anode (113,123)    SOFC (120)    Fluid metal channel lines (131,133)    Insulating layers (141,143)
NOVELTY - The plate (310) has pair of first wear resistance pieces (320) that is formed in upper and lower sides of first seating surface for preventing resistance flow. The center unit is concavely built up in inner side upper and lower portions of shear. The pair of first wear resistance pieces is individually fixed with bolt. The second combining hole is developed in second seating surface center, so that second seating surface is curved towards shaping hole (311) of shear. The pair of second wear resistance pieces (330) is individually fixed with bolt and settled in seating surface.    USE - Wheel-die type guide plate of waste extruder.    ADVANTAGE - The flowing of waste at the front side of the eccentric wheel can be prevented effectively. The generation of defects caused due to overlaying condition can be prevented. The waste of the attractive force can be reduced. The work speed can be improved and the economic inefficiency can be solved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the wheel-die type guide plate of waste extruder.    Wheel-die type guide plate (310)    Shaping hole (311)    First wear resistance piece (320)    Second wear resistance piece (330)
NOVELTY - Treating slurry comprising a digestate from a biogas plant, where biogas plant is fed a feedstock comprising about 50 to 100 wt.% of products and wastes from farms, and/or food and beverage handling, involves: (a) providing the slurry comprising a digestate from a biogas plant; (b) obtaining an acidic slurry at a pH of at most 6.5; (c) supplying the slurry with an iron salt; (d) supplying the slurry with an oxidizer selected from hydrogen peroxide and percompounds; (e) adding a flocculating polymer to the slurry obtained in (d); and (f) dewatering the slurry obtained in (e).    USE - Treating slurry comprising digestate from biogas plant (claimed).    ADVANTAGE - More efficient treatment methods are provided for digested organic material.    DETAILED DESCRIPTION - Treating slurry comprising a digestate from a biogas plant, where biogas plant is fed a feedstock comprising about 50 to 100 wt.% of products and wastes from farms, and/or food and beverage handling, involves: (a) providing the slurry comprising a digestate from a biogas plant; (b) obtaining an acidic slurry at a pH of at most 6.5, by addition of an acidic material to lower the pH of the slurry comprising a digestate from a biogas plant, if the slurry comprising a digestate from a biogas plant is not already at a pH of at most 6.5; (c) supplying the slurry with an iron salt; (d) supplying the slurry with an oxidizer selected from hydrogen peroxide and percompounds, and allowing to react; (e) adding a flocculating polymer to the slurry obtained in (d); and (f) dewatering the slurry obtained in (e), where steps (b) to (d) may be performed in any order or some or all may be performed simultaneously.
NOVELTY - A high-energy water-resistant pellet comprises: (a) at least 75% torrefied wood; and (b) the remainder of the pellet being a two-component binder comprising 2-20% by total weight of the pellet.    USE - A high-energy water-resistant pellet (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a process for making the energy pellet from torrefied wood or white wood which involves: (a) mixing at least 75% of the wood; and the remainder of the mixture being a two-component binder comprising where one component of the binder is a plasticizer selected from tall oil pitch, fatty acids, rosin, vegetable oil, animal oils and corn protein and the other component is lignin, the binder is 2-20% by total weight of the mixture; and (b) compressing the mixture by extruding the mixture at a temperature at which the binder is in a molten state to form a pellet.
NOVELTY - A biomass fuels flammable gas preparation unit has a column-shaped shell, where an upper part side of shell body and material storage chamber are connected with a feeding hopper, a left and right end of an inner cavity is provided with a combustion head, the right end is provided with an air inlet and a waste outlet, the left end of the inner cavity is provided with a punching piston and the pushing piston in order from the left to the right, the punching piston is provided with a through rod and a vent hole and one end of the through rod is connected with the punching piston.    USE - Biomass fuels flammable gas preparation unit.    ADVANTAGE - The biomass fuels flammable gas preparation unit has high efficiency.    DETAILED DESCRIPTION - A biomass fuels flammable gas preparation unit has a column-shaped shell, where an upper part side of shell body and material storage chamber are connected with a feeding hopper, a left and right end of an inner cavity is provided with a combustion head, the right end is provided with an air inlet and a waste outlet, the left end of the inner cavity is provided with a punching piston and the pushing piston in order from the left to the right, the punching piston is provided with a through rod and a vent hole, one end of the through rod is connected with the punching piston, and the other end passes through the pushing piston, a second hydraulic cylinder is connected with the pushing piston and a first hydraulic cylinder is connected with the left end of the shell and an exhaust gas outlet.
NOVELTY - Synthetic fuel comprises 92-93% methanol, 0:12-0:15% isopropyl alcohol and triethanolamine, 0:6%-0:8% hydrogen peroxide, 3-4% water, 0:03-0:05% iron naphthenate and essence.    USE - Synthetic fuel.    ADVANTAGE - The fuel has heat value of 7000 cal. It has no residual liquid, and has high heat energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of synthetic fuel comprising dissolving triethanolamine in container with hydrogen peroxide and water, adequately mixing and dissolving mixed solvent in different container with methyl alcohol, isopropyl alcohol and iron naphthenate; adding little essence; mixing and stirring uniformly, sampling and checking, and filling.
NOVELTY - Biological energy conversion natural gas combustion-supporting device comprises feeding device, air storage tank (38), gas combustion-supporting device, stirring device, and discharging device. The gas combustion-supporting device is installed on lifting gas tank. The lower part of discharging device is installed on stirring device material tray (16).    USE - Biological energy conversion natural gas combustion-supporting device.    ADVANTAGE - The device produces uniform gas temperature, and has low gas concentration of 56%. The outlet material charcoal is 99.9%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biological energy conversion natural gas combustion-supporting device.    Speed reducer (1)    Auger (2)    Fixing bracket (4)    Fan (5)    Stirring device material tray (16)    Air storage tank (38)
NOVELTY - Gas separation membrane recovery of liquid carbon dioxide (CO2) and biogas decarbonization device comprises first gas separation membrane (10) connected to secondary inlet gas separation membrane (11). The permeate side outlet gas of gas separation membrane is connected to rectifying tower (15) by CO2 compressor (12). Condenser is connected to rectifying tower top and gas mixer. The standard retentate side from secondary gas separation membrane, and permeate side of gas separation membrane is connected to mixer (18).    USE - Gas separation membrane recovery of liquid CO2 and biogas decarbonization device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas separation membrane recovery of liquid CO2 and biogas decarbonization comprising pre-processing raw material marsh gas by one-stage gas separation membrane, purifying gas retentate side to reach quality standard of natural gas, passing through secondary gas separation membrane; sending to pressurizing rectifying tower, collecting liquid CO2 from tower bottom, and returning tower top to first gas separation film for purification.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of gas separation membrane recovery of liquid carbon dioxide and biogas decarbonization device (Drawing includes non-English language text).    First gas separation membrane (10)    Secondary inlet gas separation membrane (11)    Carbon dioxide compressor (12)    Rectifying tower (15)    Mixer (18)
NOVELTY - Solid fuel comprises 50% coal, 20% charcoal powder, 10% wood cutting, 10% flue ash, additive and starch adhesive. The additive comprises sodium bicarbonate, sodium hydroxide, sodium phosphate, and/or barium nitrate.    USE - Solid fuel.    ADVANTAGE - Solid fuel material has high heat value, and it is safe and reliable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid fuel comprising crushing coal, wood powder, wood cutting, flue ash, additive, and starch into particle diameter smaller than 1 mm, mixing and stirring uniformly, grinding, shaping, and drying.
NOVELTY - Refining oil comprises (A) dissolving solid sodium hydroxide catalyst in methanol, and adjusting to proper temperature; (B) mixing with oil, and transesterifying; (C) washing with water to remove catalyst and obtain glycerol, and recycling excess methanol through distillation; (D) washing glycerol and dehydrating to obtain first nonstandard product; (E) distilling under reduced pressure to obtain second nonstandard product and heavy oil; and (F) deacidifying product, washing, and dehydrating to obtain oil according to national standards GB/T20828-2007 biodiesel products.    USE - Method for refining oil used for production of biodiesel (claimed).    ADVANTAGE - The method has stable process and less impurities on crude glycerol byproduct, achieves full recovery of excess methanol, recycles water softener, saves energy and resources, and does waste material.    DETAILED DESCRIPTION - Refining oil comprises (A) dissolving solid sodium hydroxide catalyst in methanol, and adjusting to proper temperature; (B) mixing with oil, and subjecting to transesterification reaction under suitable conditions; (C) washing with water to remove catalyst and obtain glycerol, and recycling excess methanol through distillation; (D) washing and dehydrating to obtain first nonstandard product; (E) distilling under reduced pressure to obtain second nonstandard product and heavy oil; and (F) deacidifying second nonstandard product, washing, and dehydrating to obtain oil according to national standards GB/T20828-2007 biodiesel products. The catalyst is according to national standard B209-2006IS-DTI-class product of solid sodium hydroxide.
NOVELTY - Mixing of biomass particles comprises mixing biomass particle and coal-containing fuel in coal boiler feed hopper for 1 hour; and supplying to coal combustion boiler.    USE - Method for mixing of biomass particles used for coal combustion boiler (claimed).    ADVANTAGE - The method saves cost of enterprise, reduces discharge of greenhouse gas, and greatly reduces amount of combustion products such as carbon dioxide, sulfur dioxide and nitrous oxide.
NOVELTY - The utility model claims a kind of a gasification device for producing fuel ethanol, comprising a cooler and a gas-liquid separator, the gas-liquid separator is provided with gas-liquid separating inlet and outlet, wherein the upper part of the cooler for vaporizing ethanol inlet, the lower part of the cooler is ethanol outlet and a gas outlet, a vaporizing ethanol alcohol inlet and outlet, a gas outlet of cooling coil, the alcohol outlet, a gas-liquid separating gas outlet and the inlet of the gas-liquid separator through the pipeline, a liquid cavity, a gas-liquid chamber and a liquid chamber of the gas-liquid chamber and lower part of the gas-liquid separator is divided into the upper part of the connected is connected with pipe of the gas-liquid separator, the upper end of the connecting pipe is connected with the lower part of the gas-liquid chamber, the lower end of the connecting pipe is connected with the liquid cavity is provided with a valve on the connecting pipe, is provided with discharge pipe is set on the side wall of the liquid chamber is provided with a second valve is set on the discharge pipe. Vaporizing the utility model can recycle alcohol liquid negative pressure in the filling process of the ethanol, the ethanol concentration in the air.
NOVELTY - A kind of biomass fuel system device, biomass fuel production technology field. A. providing a funnel shaped cotton stalk section of machine, the iron-removing device, a dust collecting device is set on the base of the separator, the cotton stalk section of machine, a crusher, a separating mechanism, the machine and the dryer connected in turn through a pipeline, the main control panel, comprising a biomass fuel. This utility model of the straw section only needs one person to use a forklift mechanism for feeding port in the feeding, improves the working efficiency, it is not easy to be blocked, convenient to feed and discharge. And increase dust collecting device for optimizing the power over the environment, further improves the separation quality and work efficiency, and ensures the health of the worker. Add avoids the damage of the granulating equipment except iron device. A device set, occupying the land at least, at least a power supply configured , shortens the production period and reduces the production cost.
NOVELTY - This utility model claims a kind of using moulded coal is added with domestic garbage to generate power for device, which is composed of a garbage conveying mechanism, a rolling cutter type crusher, additive delivery mechanism, clay conveying mechanism, lime conveying mechanism, a conveying mechanism, a stirrer, a pressure extrusion molding machine, a conveyor, a coal burning boiler and a generator, wherein the garbage conveying mechanism is connected with the bag breaking machine, a garbage conveying mechanism is set on the machine before the machine is connected with the rolling sieve, a rolling and knife-type crusher is connected with, pressure extrusion forming machine and the coal boiler is connected with the connecting channel is provided with a conveyor, coal burning boiler is connected with the generator, the invention has the following advantages: there is no exudates to flow, which avoids the pollution and solves the problem that the traditional garbage landfill occupying the land resource.
NOVELTY - Motor reduction box is connected with the coupling and the utility model claims a sugar cane leaf pelleting machine, the upper part of the base and connected with the vertical rotating shaft and a bearing connected with rolling wheel, the lower part of the particle forming chamber is provided with particle shape and plate shape particle collecting disc, forming annular die of biomass grain pressing plate is provided with a particle forming hole bushing, the upper part is rolling wheel working face is provided with rolling groove. A modification with a longitudinal groove according to the size and the diameter of the hole pitch of the particle forming hole on the roller working surface, which improves the pressure of the material to the traditional roller surface is light emitting surface, particle shape more easy, the granulating disc and a bearing part with a heat load to the best working state, extend a working time and service life to solve the problem of the granulator a roller pressure is small, the particle shape is difficult to forming annular die of biomass grain quality, can not work continuously for a long time and high maintenance cost and so on, it has simple structure, and it can work continuously for a long time, the maintenance cost is low.
NOVELTY - A biomass conversion catalyst (A1) in the form of particles comprises silica, clay, and a zeolite; where the particles have (i) an average pore volume of pores ranging in diameter of 80-600 Angstrom of at least 0.025 cm3/g, and (ii) an average pore volume of pores ranging in diameter of 20-80 Angstrom of not greater than 0.08 cm3/g; where each of the average pore volumes in (i) and (ii) are obtained from the adsorption branch of the nitrogen isotherm, when measured per ASTM method D4222 at 77 degrees K, and discretized according to the BJH pore size distribution model.    USE - As biomass conversion catalyst; and for the conversion of particulate biomass (claimed).    ADVANTAGE - The biomass conversion catalyst is free of or substantially free of amorphous alumina; and results in higher bio-oil yields, lower bio-oil oxygen levels, and lower coke make.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) of making a biomass conversion catalyst;    (2) biomass conversion catalyst (A2) in the form of particles comprising silica, clay, and a zeolite; where the particles have an average mesopore surface area (average MSA) of less than or equal to 50 m2/g, and where the biomass conversion catalyst has a salt concentration less than 0.1 times the mass of the silica;    (3) process for the conversion of particulate biomass involving contacting the particulate biomass with the biomass conversion catalyst (A1) or (A2) at temperatures of 200-1000 degrees C, and in the substantial absence of oxygen.
NOVELTY - Alkylation process (P1) comprises: (a) conducting alkylation reaction with ionic liquid catalyst to provide product and spent ionic liquid catalyst; (b) reacting spent ionic liquid catalyst with aluminum to provide regenerated ionic liquid catalyst and excess dissolved aluminum chloride; (c) precipitating excess dissolved aluminum chloride from regenerated ionic liquid catalyst to provide precipitated excess aluminum chloride; (d) removing precipitated excess aluminum chloride from regenerated ionic liquid catalyst; and (e) recycling regenerated ionic liquid catalyst to reaction step (a).    USE - The alkylation process is useful for removing metal halides including aluminum chloride from ionic liquids.    ADVANTAGE - The alkylation process enhances the precipitation rate of metal halides.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an alkylation process (P2), comprising: (a) and (b) as above per se; feeding the regenerated ionic liquid catalyst and dissolved aluminum chloride to a vessel (10) and providing metal halide (1) seed crystals to provide a mixture (9) comprising regenerated ionic liquid catalyst, dissolved aluminum chloride, and metal halide seed crystals; cooling the mixture in the vessel to provide precipitated aluminum chloride; removing the precipitated aluminum chloride from the vessel; and (e) as above per se.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process of removing metal halides from an ionic liquid in a crystallization vessel.    Metal halide (1)    Removed portion (3)    Heat exchanger (4)    Mixture (9)    Vessel (10)
NOVELTY - The device has a drum (1) which rotates about a shaft (2) at a different angular velocity in order to create shearing which removes the gases from several electrodes.    USE - Device for producing hydrogen and oxygen.    ADVANTAGE - As the drum rotates about shaft at different angular velocity in order to create shearing which removes the gases from several electrodes, the combustion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing hydrogen and oxygen.    Drum (1)    Shaft (2)    Entrance hole (10)    Chamber (11)    External connection (17)
NOVELTY - Organic fuel synthesis plant is claimed.    USE - The organic fuel synthesis plant is useful to form a synthesis gas that is used to produce hydrocarbons and alcohols, where the organic materials are used for industrial processes, for the fabrication of plastics and similar materials, fiber-reinforced composites, and pharmaceutical products (all claimed).    ADVANTAGE - The organic fuel synthesis plant utilizes solar energy to produce organic fuels from water and carbon dioxide.
NOVELTY - An apparatus consists of bioreactor, pre-depositing tank provided with calcium hydroxide mixing tank and feeding device, flocculation tank provided with propeller mixer, ferric(III) chloride mixing tank and feeding device, lamellar depositor, ozonizer, deozonizer, sludge storage tank, sludge digestor, gas storage tank, composter, and membrane filter in which pore size of membrane is 0.2 m. The bioreactor has anox and aeron membrane spaces in ratio of 1/3:2/3.    USE - Apparatus is used for cleaning communal wastewater, recycling gained water, and utilizing separated organic contamination for producing biogas.
NOVELTY - City civil sewage deposition treatment is carried out to obtain sludge with a moisture content of 60-70%. 5-6 Wt.% calcium oxide and 4-6 wt.% sodium hydroxide are added to sludge and stirred for 10 minutes, and moisture content is reduced to 50%. The treated sludge is sent to a deodorizing stirring tank, 2 wt.% sludge stabilizer is added, and the mixture is stirred for 10 minutes. The mixture is loosened to obtain stable sludge. Finished sludge, coke foam, coal gangue, biomass powder, and additive are mixed to obtain a mixed fuel powder.    USE - Flammable solid-liquid deposition (claimed).    ADVANTAGE - The method provides mixed fuel powder having excellent combustion quality.    DETAILED DESCRIPTION - City civil sewage deposition treatment is carried out to obtain sludge with a moisture content of 60-70%. 5-6 Wt.% calcium oxide and 4-6 wt.% sodium hydroxide are added to sludge and stirred for 10 minutes, and moisture content is reduced to 50%. The treated sludge is sent to a deodorizing stirring tank, 2 wt.% sludge stabilizer is added, and the mixture is stirred for 10 minutes. The mixture is loosened to obtain stable sludge. 30-40 Parts mass finished sludge, 20-30 parts mass coke foam, 5-10 parts mass coal gangue, 15-25 parts mass biomass powder, and 8-10 parts mass additive are mixed in a tubular automatic mixer for 10 minutes to obtain a mixed fuel powder. An INDEPENDENT CLAIM is included for flammable solid-liquid deposition device consisting of a liquid-solid inlet, a storage bin, a separating agent-additive delivery system, a deodorizing stirring tank, a biomass powder-additive delivery system, and a finished-material mixing tank.
NOVELTY - Coke oven gas hydrogen production comprises pre-purifying coke-oven gas, removing naphthalene, feeding into pressure swing adsorption (PSA)-1 with 12 towers, removing most carbon dioxide, feeding into PSA-2 with 10 absorption towers, removing most methane gas, pressurizing obtained hydrogen-rich gas to 2.6 MPa, cooling hot compressed gas in deoxidizing system, and performing hydrogen purification.    USE - Method for producing Coke oven gas hydrogen (claimed).    ADVANTAGE - Hydrogen output reaches 99.9% generating 40110 Nm3/hour from 50000 Nm3/hour coke oven gas. Thermal value of mixed gas 4276-4636 kcal/Nm3.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of coke oven gas hydrogen production (Drawing includes non-English language text).
NOVELTY - This utility model claims a kind of of alkyl gas hydro-condensed liquid ethane component of a device, comprising a tower, a liquid pipe, air of air pipe, the tower top gas pipeline and tower kettle liquid phase discharging pipe, the recycling tower for gas stripping tower, the condensed liquid pipe one end of which is connected with the gas stripping tower, wherein the gas stripping and the air of air pipe is provided with a control valve proceeded by the lower part of the air pipe and the gas stripping tower, the tower top gas pipeline is provided with a tower top pressure control valve, one end of which is connected with the air tower top and the other end is connected with the product gas pipeline, the tower kettle liquid phase discharging pipe one end of which is connected with the gas stripping tower bottom, and the other end is connected with the light oil system, and is provided with a liquid control valve is set on the tower kettle liquid phase discharging pipeline. The utility model can further recycle ethane, propane gas in the condensed liquid, improves the yield of the ethane, propane, and the utility model has small size, and the operation is simple.
NOVELTY - This utility model claims a kind of alkyl dry gas purifying refining device, comprising a hydrogenation reaction system, heat recovery system, a liquid recycling system, the hydrogenation reaction system comprising a reactor, starting a heater and a cooler, a gas-liquid separator, heat recycling system comprises a material inlet and outlet heat exchanger, a steam generator and a steam over-heater, the condensed liquid recycling system comprises a condensed liquid gas stripping tower, the inlet and outlet material heat exchanger, starting the heater, a reactor, a steam over-heater, a steam generator, a material inlet and outlet heat exchanger, a cooler, a gas-liquid separator connected in turn according to the order, and said gas-liquid separator by pipeline through a pressure reducing valve A and the condensing liquid gas stripping tower. This utility model is a combined catalytic hydrogenation method to remove the harmful impurity in the product of dry gas and ensure the quality of the product as the safety of ethylene raw material, and a system for recovering the heat and the heat, saving energy and reducing consumption, a condensed liquid recycling system and further improves the product yield.
NOVELTY - Sewage treatment involves crude processing, sedimenting sludge, producing biogas, and sludge dewatering.    USE - Sewage treatment used for producing biogas.
NOVELTY - Marsh gas purification process for preparing natural gas, involves: (1) marsh gas wet desulfurization and dry desulphurization to remove hydrogen sulfide and carbon dioxide in marsh gas and to obtain desulfurized marsh gas; (2) separating the desulfurized marsh gas by water, compressing, cooling for thick dehydrating and then fine dehydrating with molecular sieve to obtain dehydrated marsh gas; and (3) carrying out refrigeration process for cooling dehydrated marsh gas, and condensing carbon dioxide in dehydrated marsh gas into liquid, to obtain liquid natural gas and carbon dioxide.    USE - For marsh gas purification process for preparing natural gas (claimed).    ADVANTAGE - The process has simple operation, and has low biogas methane component loss rate. The natural gas prepared by this process meets the national standard, which can meet the usage requirement of the compressed natural gas of vehicle. The process not only greatly improves the additional value of the product of the marsh gas, but also expands the marsh gas use range; and provides obvious economic benefit and greatly broadens the target market of the marsh gas. The marsh gas purification method plays an active role, to solve the energy crisis, and in energy conservation and protection of the environment; and provides great social benefits.    DESCRIPTION OF DRAWING(S) - The figure shows a flow chart of the dehydration, decarburization process.
NOVELTY - A catalytic composite electrode comprises nickel hydroxide (Ni(OH)2), nickel sulfide (Ni3S2), and nickel (Ni) foam in which Ni(OH)2 is a thin outer layer film, Ni3S2 nanoparticles is active material, and Ni foam is a conductive substrate.    USE - A catalytic composite electrode for electrolyzing water in alkaline oxide (claimed).    ADVANTAGE - Product has ultra-low electric potential and high current density, and significantly reduces power consumption. Preparation method is simple and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalytic composite electrode which involves pre-treating nickel or nickel source successively with deionized water, alcohol, and acetone, ultrasonically cleaning to remove surface organics in which nickel or nickel source is a foamed nickel sheet, dipping in aqueous solution of sulfur source, autoclaving at 140-200 degrees C in hot water for 1-8 hours, cooling, taking out, rinsing with deionized water, drying in vacuo at 60-100 degrees C for 12-24 hours in which sulfur source is sulfur thioacetamide, thiourea or sodium sulfide.    DESCRIPTION OF DRAWING(S) - The drawing shows an electrode polarization curve of catalytic composite electrode. (Drawing includes non-English language text).
NOVELTY - The incinerator (2) has an air heating chamber (70) which heats combustion air with combustion heat of waste material in combustion space (2a). Furnace main-portion (20) is provided with cylindrical space section. The air heating chamber is provided so that portion of space section of cylindrical-axle direction is enclosed in circumferential direction. The channel area of combustion air in air heating chamber is narrowed. Baffle plate is formed to restrict flow along circumferential direction of cylindrical space portion of combustion air in air heating chamber.    USE - Dry-distillation incinerator of dry distillation type incineration system (claimed), for dry-distilling combustible waste material. Uses include but are not limited to combustible waste material such as waste tire, plastics, medical waste, shredder dust, wood chip, general refuse, and waste oil.    ADVANTAGE - Since the baffle plate is formed to restrict flow along circumferential direction of cylindrical space portion of combustion air in air heating chamber, the increase in the speed of combustion and the reduction of the residual amount of the ashes after combustion can be achieved and the process performance of waste material can be improved by simple structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a dry distillation type incineration system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the dry-distillation incinerator.    Dry-distillation incinerator (2)    Combustion space (2a)    Furnace main-portion (20)    Air heating chamber (70)    Introductory piping portion (80)
NOVELTY - A peptide comprising a 12 amino acid sequence (SEQ ID NO: 1-3) fully defined in the specification, is new. The peptide has saccharification residue component bonding ability.    USE - The peptide is useful as saccharification residue component adsorption agent. The saccharification method is useful for producing ethanol using the peptide (all claimed).    ADVANTAGE - The peptide improves saccharification efficiency by saccharogenic amylase. The method prevents inhibitory effect of saccharogenic amylase by saccharification residue component adsorption agent at low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) saccharification residue component adsorption agent comprising the peptide; and    (2) saccharification method involves saccharifying cellulose biomass with saccharogenic amylase in presence of the peptide and/or saccharification residue component adsorption agent.
NOVELTY - Purifying mixed gas comprises subjecting the mixed gas to two reaction branches for alternatively performing hydration reaction and decomposition reaction, carrying out hydration reaction in one reaction branch and carrying out decomposition reaction in the other one reaction branch, where the heat generated in the hydration reaction is released and used in the decomposition reaction in the other reaction branch, separating water and gas to form hydrate, separating gas from the other mixed gases, and decomposing the hydrate to obtain purified gas.    USE - The method is useful for purifying mixed gas (claimed).    ADVANTAGE - The device: carries out mixed gas purification in a continuous manner with low energy consumption. The method has high safety; and enables each component to form a hydrate in the mixed gas based on the pressure and temperature difference.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for purifying mixed gas, comprising a reactor (7) provided with two reaction branches, where one reaction branch is provided with an air inlet and an air outlet. The upper part of each reaction branches are adapted to alternately carry out hydration reaction and decomposition reaction, where first reaction branch sidewall allows heat exchange with the second branch to utilize the heat released by the first reaction branch during hydration reaction for decomposition reaction in the other branch.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for purifying mixed gas.    Negative pressure suction pump (3)    Inlet (6)    Reactor (7)    Cooling water tank (11)    Compressor (12)
NOVELTY - A biomass solid fuel contains 90 wt.% biomass raw materials which is crop waste, bamboo-wood processing residue, tree felling and residual branch leaves, and 10 wt.% moisture.    USE - Biomass solid fuel (claimed).    ADVANTAGE - Biomass solid fuel is environment-friendly, suitable for industrialized production, saves transportation cost and utilization ratio, completely uses heat energy, and uses renewable energy source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass solid fuel which involves crushing and sieving raw materials to powder, or granular particles with 4 mm diameter using crusher, or screen sieving powder raw materials, drying using drying device to 13-18% moisture, continuously drying using special spark-extinguishing device, separating material, water vapor and air using dedicated separating system, transporting separated materials and dust to recovery region, mixing 90 wt.% raw materials with 10 wt.% water, stirring to obtain uniform moisture, subjecting to granulating molding using biomass solid press to form small square blocks with 6-20 mm, length of 1-10 mm and side length of 33 mm, or cylindrical solid fuel with 70-80 mm diameter, or 3-20 mm length, cooling to 35 degrees C and uniformly packaging.
NOVELTY - Conjugated linoleate is prepared from vegetable oil biodiesel by pre-esterifying (S1), transesterifying (S3) oil phase by microwave heating to 60-85 degrees C, adding homogeneous base catalyst, 1st oil phase, and alcohol solution to obtain pre-esterified vegetable oil phase in which homogeneous base catalyst is 0.8-1.5 wt.%, and mole ratio 1st oil phase:alcohol is 5-12, and separating biodiesel by cooling.    USE - Preparation of conjugated linoleate from vegetable oil biodiesel (claimed).    ADVANTAGE - The preparation of conjugated linoleate from vegetable oil biodiesel is environment-friendly, shortens transesterification time, enhances production capacity, and improves biodiesel production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of preparation of conjugated linoleate from vegetable oil biodiesel. (Drawing includes non-English language text).    Pre-esterification (S1)    2nd separation (S2)    Transesterification (S3)    1st separation (S4)
NOVELTY - Biodiesel extraction involves using Thevetia peruviana seed in hexane solvent in a mechanical medium with a hydraulic press to obtain an oil. The obtained oil is filtrated in an activated carbon column, and is subjected to a conversion process from vegetable oil to biodiesel, preferably transesterification.    USE - Method for extracting biodiesel.    ADVANTAGE - The method provides biodiesel having specific properties in a convenient manner.
NOVELTY - The hydrogen oxygen mixing gas generator has an electrode (2) in which an outer periphery of a carbon nano is plated. An electrode (1) is configured to maintain the fixed gap. The carbon nano is plated is numerously connected and is formed in the inner periphery. An insulator (22) of the ring type is installed at the exterior of an electrode (21) and is configured to insulate the electrode (1). A hole is configured for indignant with water and to release the heat generated in the electrode (1).    USE - Hydrogen-oxygen mixing gas generator of hydrogen oxygen mixing gas generate system for electrolyzing water.    ADVANTAGE - The hydrogen oxygen mixing gas generator can irradiate the electromagnetic wave like the gamma-ray besides the carbon nano function and is well put through electricity and can maximize amount of the hydrogen oxygen mixing gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen oxygen mixing gas generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen-oxygen mixing gas generator.    Electrodes (1,2,21)    Insulator (22)
NOVELTY - An iridium metal ring photosensitizer comprises bibenzimidazole-containing compound.    USE - An iridium metal ring photosensitizer for photocatalytic reduction of water (claimed).    ADVANTAGE - Dual-core iridium photosensitizer has higher activity compared to single-core iridium photosensitizer and good photocatalytic performance.    DETAILED DESCRIPTION - An iridium metal ring photosensitizer comprises bibenzimidazole-containing compound of formula (I). INDEPENDENT CLAIMS are included for:    (1) preparation of iridium metal ring photosensitizer which involves placing chlorine bridge dimer ((Ir(tfmppy) ( mu -Cl))2) and bibenzimidazole in double mixed solvent of methanol and methylene dichloride, adding sodium carbonate (Na2CO3), performing reflux, cooling, drying solvent using rotary dryer, and passing through column in which eluent is ethyl acetate and n-hexane with ratio of 1:1 with respect to pure ethyl acetate; and    (2) catalytic reduction of water which involves dissolving iridium, electronic agent which is triethanolamine and catalyst which is tris(bipyridine)cobalt(II) ion ((Co(bpy)3)2+), potassium tetrachloroplatinate(II) (K2PtCl4), cobalt(II) chloride (CoCl2), or tris(4,4'-di-tert.-butyl-2,2'-dipyridine)cobalt(III) ion (Rh(dtbpy)3)3+, and lithium chloride (LiCl) in aqueous solution, adjusting pH to 8 using concentrated hydrochloric acid, and preparing hydrogen under the irradiation of visible light.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of nuclear magnetic hydrogen spectrum of compound.
NOVELTY - A fertilizer contains humic acid, water-absorbing polymer material, and organic fertilizer.    USE - Fertilizer for improving moisture-retention of soil (claimed).    ADVANTAGE - The fertilizer is low-cost, improves soil salinity, increases moisture retention, reduces sodium and chloride content, soil adsorption ratio, and de-icing of soil, promotes growth and helps maintain green plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer which involves fermenting compost to obtain organic fertilizer, mixing humic acid, and water-retaining polymer material, and grinding to obtain spherical or rod-shaped fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of different environmental impacts of fertilizer on growth secondary cypress branch. (Drawing includes non-English language text).
NOVELTY - Producing yellow humic acid organic fertilizer, comprises crushing peat and adding wheat bran to obtain a mixture, adding active sludge and water to the mixture, performing anaerobic fermentation of the mixture to obtain marsh gas, performing methane fermentation, crushing and sieving obtained residue to obtain mixed product, adding acetone solution, distilled water and concentrated sulfuric acid to the mixed product and stirring, filtering the product to obtain yellow humic acid residue, adding auxiliary materials to the residue, and drying.    USE - The method is useful for producing yellow humic acid organic fertilizer (claimed).    DETAILED DESCRIPTION - Producing yellow humic acid organic fertilizer, comprises crushing peat and adding wheat bran at a pH of 6.5-7.5 to obtain a mixture, where the wheat bran comprises a carbon to nitrogen ratio of 25-30:1, adding 10-80% of active sludge and water to the mixture, where the solid to liquid ratio is 1-20:1, performing anaerobic fermentation of the mixture at 15-58 degrees C for 1-50 days to obtain marsh gas, performing methane fermentation at 60-110 degrees C for 4 hours, crushing and sieving obtained residue at room temperature to obtain mixed product, adding 50-300% of acetone solution, 100-300% of distilled water and 10-150% of concentrated sulfuric acid to the mixed product and stirring for 0.5-3 hours, preferably 2-6 hours, filtering the product to obtain yellow humic acid residue, adding auxiliary materials to the residue by adjusting the pH to 6.5-7.5 with sodium hydroxide solution, and drying.
NOVELTY - The method involves partially converting solid material to carbon monoxide and hydrogen by a gasification process, and separating aqueous water current from flow of gas. Water purification is subjected to the water current and isolated into three degrees of purity. First stream of water is provided with a highest degree of purity. A vapor generation with second stream of water, is supplied to medium purity having solids slurry. Ash introduced into a gasification reactor (10) is fed to third water stream having lowest degree of purity and returned into solid material gasification.    USE - Method for gasification of carbonaceous solid material such as charcoal or biomass.    ADVANTAGE - The method enables isolating water purification into three degrees of purity so as to reduce effluent generation during solid material gasification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plant for gasification of carbonaceous solid material.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a plant for gasification of carbonaceous solid material.    Spacer (1)    Gasification reactor (10)    Gas cooler (20)    Ammonia recovery unit (25)    Water purification unit (30)
NOVELTY - Torrefaction of biomass in a torrefaction system with at least one torrefaction reactor (8) using torrefaction gas (9), which is produced during torrefaction, comprises combusting the torrefaction gas with a water-steam-cycle in a power plant coupled with the torrefaction reactor as secondary fuel, and at least partially decoupling energy required for torrefaction from the power plant.    USE - The method is useful for torrefaction of biomass in a torrefaction system.    ADVANTAGE - The method is carried out in a cost efficient and energy efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above mentioned method, comprising the torrefaction reactor, at least a steam generator (1) and at least one turbine, which is operated with steam from the water-steam cycle of the steam generator, where the torrefaction reactor is directly or indirectly coupled thermally to the steam generator.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device.    Steam generator (1)    Primary air (4)    Secondary air (5)    Torrefaction reactor (8)    Torrefaction gas (9)
NOVELTY - Torrefaction of biomass in a torrefaction system with at least one torrefaction reactor (3) using torrefaction gas, which is produced during torrefaction, comprises combusting the torrefaction gas in a power plant coupled with the torrefaction reactor or a heating plant as secondary fuel, and at least partially decoupling energy required for torrefaction from the power plant or the heating plant. A part of thermal energy decoupled from the power plant or the heating plant is used for drying biomass to the second fuel, which exhibits volume- or mass-specific energy density.    USE - The method is useful for torrefaction of biomass in a torrefaction system.    ADVANTAGE - The method is carried out in a cost efficient and energy efficient manner.    DETAILED DESCRIPTION - Torrefaction of biomass in a torrefaction system with at least one torrefaction reactor (3) using torrefaction gas, which is produced during torrefaction, comprises combusting the torrefaction gas in a power plant coupled with the torrefaction reactor or a heating plant as secondary fuel, and at least partially decoupling energy required for torrefaction from the power plant or the heating plant. A part of thermal energy decoupled from the power plant or the heating plant is used for drying biomass to the second fuel, which exhibits volume- or mass-specific energy density different from the torrefied biomass.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a plant for torrefaction of biomass for the production of pelleted dried biomass.    Drum dryer (2)    Torrefaction reactor (3)    Heat exchanger (7)    Mixing chamber (8)    Hammer mill (9)
NOVELTY - The bridge elimination control apparatus has a stirring element (31) which is inserted into inner cylinder (23) to make up-down direction of gasifier (20) in longitudinal direction. A raising/lowering driving unit is provided to raise/lower stirring element in stand-by position (X) that is apart from solid raw material (5) in inner cylinder. A rotational drive unit is provided to rotate stirring element around stirring element shaft (33). A control apparatus controls raising/lowering driving unit and rotational drive unit based on signal of detection unit (25,26a-26c,27a-27c).    USE - Bridge elimination control apparatus of gasifier in biomass gasification system used for gasifying biomass fuel.    ADVANTAGE - Since the control apparatus controls the raising/lowering driving unit and rotational drive unit based on signal of detection unit, the occurrence of bridge in the gasifier can be eliminated effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of gasifier with stand-by position of stirring blade.    Solid raw material (5)    Gasifier (20)    Inner cylinder (23)    Detection units (25,26a-26c,27a-27c)    Stirring element (31)    Stirring element shaft (33)    Stand-by position (X)
NOVELTY - This utility model claims a kind of extracting low-concentration oxygen-containing coal bed methane, comprising a heat exchange system, a rectifying and separating, a mixed refrigerant circulating system and a nitrogen cold agent circulating system. Heat exchange system comprises a primary heat exchanger along the gas flow direction, a two-grade heat exchanger, a heat exchanger and a heat exchanger, rectifying and separating system comprises a rectification tower, the evaporator of the rectification tower and the condenser and the separator tower top of the rectifying tower, a refrigerant cycle system comprises a refrigerant flow direction of a refrigerant compressor, a refrigerant cooler and a refrigerant separating tank of nitrogen cooling agent circulation system comprises a nitrogen cooling agent flow in turn is provided with a nitrogen cooling agent compressor and nitrogen cooling agent. At the same time this utility model can obtain high heat exchange efficiency, and also has good adaptability and operability of the working condition change of extracting methane, and also capable of preventing a blocked refrigerant pipeline.
NOVELTY - The device has a main body provided with a methane sensing element, an amplifying circuit, an A/D converting circuit, a micro-processor, an alarm circuit, a display circuit and a power supply. The sensing element, the amplifying circuit, the A/D converting circuit and the micro-processor are connected with each other, where the methane sensing element is a black and white heat catalysis element. The alarm circuit and the display circuit are connected with the microprocessor. The power supply is a 3.6 nickel-hydrogen battery.    USE - Air methane and carbon monoxide concentration measuring device.    ADVANTAGE - The device is hung on a to-be-detected place, and enables the alarm circuit to generate alarm and the display circuit to display current air methane and carbon monoxide concentration value when methane and carbon monoxide concentration in air exceeds a certain degree.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an air methane and carbon monoxide concentration measuring device.'(Drawing includes non-English language text)'
NOVELTY - Catalytic pyrolysis of biomass oil comprises mixing pulverized biomass solids and ceramic solid acid catalyst at mass ratio of 2.3-9 in reactor, preheating, and drying; and subjecting to pyrolysis at 550 degrees C to generate gaseous product, and condensing to obtain biomass pyrolysis oil. The ceramic solid acid catalyst is tungsten-zirconia (WO3-ZrO2) ceramic solid acid catalyst, tungsten-alumina (WO3-Al2O3) ceramic solid acid catalyst, or tungsten-tin oxide (WO3-SnO2) solid acid catalyst.    USE - Method for catalytic pyrolysis of biomass oil (claimed) used as fuel for thermal power plants and boilers, and base chemical raw material.    ADVANTAGE - The method improves yield by 20-30%.
NOVELTY - An environment-friendly bioliquid fuel comprises 55-75 pts. wt. animal and vegetable oils, 15-20 pts. wt. eicosapentaenoic acid, 10-12 pts. wt. methylal, 5-10 pts. wt. fatty acid methyl ester, 0.5-3 pts. wt. triethylamine, 0.1-2 pts. wt. taste masking agent, and 0.05-1.5 pts. wt. hydrazine.    USE - Environment-friendly bioliquid fuel used as fuel for boiler and power plant.    ADVANTAGE - The fuel achieves national standard indicator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fuel by mixing animal and vegetable oils, methylal, and fatty acid methyl ester; mixing eicosapentaenoic acid and hydrazine; mixing two mixtures, adding triethylamine and taste masking agent, and uniformly mixing.
NOVELTY - This utility model using the methanation gas to synthesis tower cooling device, referring to a heat exchange device, which is composed of a synthesis gas compressor, a synthetic tower, small synthetic tower, ammonia-cooling device I and a liquid ammonia separator, a synthesis gas compressor through synthesizing tower outlet gas heat exchanger and synthetic tower synthetic tower through the small synthetic tower, boiler water and the synthesis gas heat exchanger and the synthesizing tower outlet gas heat exchanger shell side pipeline, the synthesizing tower outlet gas heat exchanger shell side by synthesis gas with the circulating water heat exchanger is respectively connected with the ammonia-cooling device I and a synthesis gas with ammonia steam heat exchanger pipe side of the ammonia cooler I and a synthesis gas with ammonia steam heat exchanger tube side outlet are connected with the ammonia-cooling device II and the liquid ammonia separator pipe, a liquid ammonia separator is connected with a synthesis gas with ammonia steam heat exchanger shell side of the synthesis gas with ammonia steam heat exchanger shell side of the synthesis gas compressor pipeline is connected to form a loop. The device has simple structure, shortens the time of the synthesis tower, increasing the safety and reliability of the device, and improves the service life of the whole device.
NOVELTY - This utility model claims a kind of using absorption-rectification combined purifying n-butyl alkyl of device, the n-butane by absorbing a NaX adsorbent, a rectifying tower for pumping process, then the adsorber outlet disposable feeding into the tower, the tower top by ice salt condensing agent to control the temperature, the kettle tower is a water bath to control the temperature. At last the lower in a tower operation, the tower kettle product in filled steel bottle, for producing high pure butane with the technology has fast separating speed, simple device, convenient operation, and reliable device, which is suitable for small dosage, high purity of production.
NOVELTY - This utility model claims a kind of mobile coalbed methane purifying device, comprising a particulate filter, a dehydrating device, a carbon dioxide removing device, a liquefying device, fractionating device and an air storage tank, an air outlet end of the particle filter is connected with a gas inlet end of the dewatering device, air outlet end of the dewatering device is connected with the air inlet end of the sulphur and carbon dioxide removing device is connected with the air outlet end of the sulphur and carbon dioxide removing device is connected with the air inlet end of the compressing and liquefying device, a liquefying device connected with the air outlet end of the air inlet end of the fractionating device, an air outlet end of the fractionation device is connected with the air storage tank is connected with the air inlet. This utility model is a liquefying and separating are complete at low temperature, separating high purity and good safety performance, wherein a separating air outlet at the same time for preparing liquefied natural gas, which effectively uses the coal bed gas source, which avoids the air pollution caused by discharging. A complete set of device is installed on a container in the container, and it can move and transport.
NOVELTY - Cosmetic water-in-oil emulsion comprises (a) cetyl polyethylene glycol/polypropylene glycol-10/1 dimethicone, and (b) 2,4-bis-((4-(2-ethyl-hexyloxy)-2-hydroxy)phenyl)-6-(4-methoxyphenyl)-1,3,5-triazine.    USE - The cosmetic water-in-oil emulsion is useful as sunscreen lotion.    ADVANTAGE - The cosmetic water-in-oil emulsion exhibits good sprayingability, improved temperature- and storage- stability, and provides velvety or silky skin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a propellant gas can containing an aerosol spray, where the can is an aluminum can coated on an inside with a protective coating.
NOVELTY - A sewage treatment system comprises collecting tank, biogas tank, biogas tank feeding port, anti-seepage layer, biogas fermentation tank, biogas slag layer, biogas slag outlet, liquid outlet, slag discharging tank, slurry collecting tank and biogas purifying system.    USE - Sewage treatment system.    ADVANTAGE - The system has reasonable pipeline design, automatic slag separation, high utilization rate, low construction cost, high economical benefit and easy large-scale implementation.
NOVELTY - A lignocellulose material as raw material is subjected to hydrothermally-treatment and/or dehydration, compression process and drying, to obtain solid fuel.    USE - Manufacture of solid fuel (claimed).    ADVANTAGE - The method enables manufacture of solid fuel having high energy density.
NOVELTY - Digestate treatment system (1), comprises a separating device (3) for separating a supplied digestate into a liquid phase and a solid phase, an evaporator unit for separating the liquid phase into water, a first phase manure and solid residues, preferably by supply of low-temperature thermal energy and a briquetting device for pressing the solid phase into the briquette shape.    USE - Used as a digestate treatment system.    ADVANTAGE - The digestate treatment system: saves maintenance and operating costs; completely decomposes the digestate into its components; and improves the quality of digestate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for processing digestate, comprising providing a digestate, separating the digestate into a liquid phase and a solid phase, separating the liquid phase into water, a first phase manure and solid residues by supplying low-temperature thermal energy, and pressing the solid phase into briquette shape.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the digestate treatment system.    Digestate treatment system (1)    Separating device (3)    Shaft (5)    Transport medium (7)    Liquid phase line (9)
NOVELTY - Substituted morpholin-4-ium compound (I), is new.    USE - The (I) is useful as a gas hydrate production promoter.    ADVANTAGE - The (I) effectively improves production of gas hydrate.    DETAILED DESCRIPTION - Substituted morpholin-4-ium compound of formula (I), is new.    R1, R2 = linear or branched 1-3C-alkyl or straight or branched chain 1-3C-hydroxyalkyl.    An INDEPENDENT CLAIM is included for a method for promoting gas hydrate generation using (I).
NOVELTY - Method (M1) for degrading cellulose or lignocellulosic biomass, involves contacting a cellulose containing material or lignocellulosic biomass with an enzyme cocktail comprising a thermostable enzyme having a glycoside hydrolase 9 (GH9) domain and a GH48 domain, and a thermostable beta glucosidase.    USE - The method (M1) and enzyme cocktail are useful for degrading cellulose or lignocellulosic biomass. The method (M2) and enzyme cocktail are useful for producing a biofuel from lignocellulosic biomass (claimed), e.g. ethanol. The method (M1) is useful for producing higher alcohols, hydrocarbons, or other advanced fuels from cellulose. The enzyme cocktail is useful for degrading (e.g. by liquefaction) a variety of cellulose products (e.g. paper and cotton) in landfills, enhancing cleaning ability of detergents, and improving feel of cotton fabrics (e.g. stone washing and biopolishing), as a softening agent and in feed compositions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) enzyme cocktail comprising Caldicellulosiruptor bescii CelA, a thermostable beta glucosidase, and a thermostable endoglucanase; and (2) method (M2) for producing a biofuel from lignocellulosic biomass involves (a) contacting the biomass with the enzyme cocktail, and (b) converting the sugars to biofuel by fermentation.
NOVELTY - A biomass biomass fuel oil production method involves selecting pine raw material, crushing, drying material till water content reaches less than 8%, treating in a pyrolysis reactor at 480-530 degrees C, maintaining internal pressure at 500 Pa, feeding material at 12 ton/hour, cooling to less than 60 degrees C and separating resultant product to obtain fuel oil.    USE - Method for producing biomass fuel.    ADVANTAGE - The method enables producing biomass fuel with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a purifying device comprising a fluidized bed regenerator, an inertial separator, a pyrolysis reactor, semi-coke material returning device connected to form a circulating system, where the inertial separator is connected with a cyclone separator, the lower outlet of the cyclone separator is connected with returning fluidized bed regenerator through heat carrier, the semi-coke separator of the pyrolysis gas outlet is connected with the spray tower, the spray tower is provided with a spraying opening, the top portion is set with the pyrolysis dry gas outlet, and the bottom portion is provided with a fuel oil outlet.
NOVELTY - Use of chlorine dioxide solution blocking agent in coal seam gas mining, is claimed, where the modified coal methane adsorption capacity and permeability.    USE - The chlorine dioxide solution blocking agent is useful in coal seam gas mining (claimed).    ADVANTAGE - The chlorine dioxide solution blocking agent has exhausted pressure recovery ratio of the coal bed gas.
NOVELTY - A synthetic fuel comprises 92-93% methanol, isopropanol, 0.12-0.15% triethanolamine, 0.6-0.8% hydrogen peroxide, 3-4% water, 0.03-0.05% iron naphthenate, and essence.    USE - Synthetic fuel for rural area combustion (claimed).    ADVANTAGE - The fuel is nontoxic, environment-friendly, and low cost, and has high heat value and no combustion residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of synthetic fuel which involves stirring triethanolamine in container, mixing hydrogen peroxide and water in another container, mixing 2 solutions, adding methanol, isopropanol, water, iron naphthenate, and essence, uniformly mixing, performing sampling inspection, and filling for storage.
NOVELTY - Pretreating (I) lignocellulosic biomass prior to enzymatic hydrolytic saccharification, comprises: (a1) mixing the biomass with hydrogen peroxide solution prepared in water to form 0-90 wt/wt.% moisture content of biomass; and (a2) exposing the biomass/hydrogen peroxide mixture to ozone gas at 15-30 degrees C.    USE - The method is useful for pretreating lignocellulosic biomass prior to enzymatic hydrolytic saccharification. The produced biomass with lower lignin concentration is suitable for simultaneous saccharification and fermentation process of any biofuel or byproduct. The method is also useful for production of sugars (all claimed) for microbial lipid (e.g. biofuel) production.    ADVANTAGE - The method: utilizes low amount of pretreatment reagents (ozone, hydrogen peroxide, and ammonia), and for recycling the reagents; and utilizes low temperature and pressure conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) pretreating (II) biomass prior to enzymatic hydrolytic saccharification, comprising: exposing the biomass to ozone at a temperature of 15-30 degrees C; and contacting ozone-exposed biomass with aqueous ammonia at a temperature of or below 50 degrees C and pressure lower than 1 atmosphere; and    (2) pretreating (III) biomass prior to hydrolytic saccharification, comprising steps (a1) and (a2) as above per se, and then contacting ozone-treated biomass with aqueous ammonia at a temperature of or below about 50 degrees C.
NOVELTY - Production of syngas, (1) comprises: forming a gaseous reactant mixture comprising a hydrocarbon fuel; and reforming the reactant mixture in a reforming reactor (35) at a target reforming temperature to produce hydrogen gas, where the reactant mixture is heated by a heat transfer fluid which, prior to heating the reactant mixture, passes through a solar energy receiver (15), where the volumetric ratio of heat transfer fluid between the receiver and the reforming reactor to the heat transfer fluid in the receiver is less than 50.    USE - The process is useful for producing syngas (claimed) which is useful for producing methane ethanol and/or methanol.    ADVANTAGE - The process utilizes an apparatus which responsively controls reforming reactor temperature using a relatively small amount of heat transfer fluid, thus minimizing heat losses and improving overall solar energy conversion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for the production of syngas comprising: a solar energy (10) receiver for receiving solar energy and transferring the energy to the heat transfer fluid; and a reforming reactor for reacting the gaseous reactant mixture comprising a hydrocarbon fuel and water.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the process for producing syngas.    Syngas (1)    Solar energy (10)    Solar energy receiver (15)    Tower (20)    Reforming reactor (35)
NOVELTY - The apparatus has a gasifier which gasifies gasification raw material using water vapor and generates gasifying gas. A circulation path (210) is provided in which the gasifying gas generated in the gasifier is circulated. Primary catalyst holding portion (220) is provided for stimulating reformation of tar in gasifying gas and for holding primary catalyst containing nickel (Ni) in the circulation path. An oxidizing agent supply portion (230) is arranged for supplying an oxidizing agent to primary catalyst.    USE - Apparatus for generating gasifying gas by gasifying gasification raw material such as unused fuel, coal, biomass and tire tip.    ADVANTAGE - The gasifying gas generation apparatus can suppress the reduction of combustible gas. A tar reforming apparatus can efficiently remove the tar.    DETAILED DESCRIPTION - The apparatus has an oxidizing agent control portion (250) that controls quantity of oxidizing agent according to temperature of primary catalyst measured by temperature measurement portion (240). A bypass is arranged for bypassing gasifying gas of upstream of secondary catalyst holding portion. A pressure-loss measurement portion measures pressure loss in primary catalyst. A switching control portion is provided for switching circulation destination of gasifying gas to bypass, when measured pressure loss is less than predetermined threshold value.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the tar reforming apparatus. (Drawing includes non-English language text)    Circulation path (210)    Primary catalyst holding portion (220)    Oxidizing agent supply portion (230)    Temperature measurement portion (240)    Oxidizing agent control portion (250)
NOVELTY - Preparing biodiesel comprises: carrying out contact reaction of a grease raw material and monohydric alcohol to obtain a mixture containing crude fatty acid monoalkyl ester; passing the mixture containing crude fatty acid monoalkyl ester into a flash tower to carry out flash evaporation for dehydration, thus obtaining a monohydric alcohol-water gas mixture; and carrying out contact reaction on the crude fatty acid monoalkyl ester in the dehydrated mixture and the monohydric alcohol.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method can efficiently and steadily lower the acid value of the biodiesel product and enhance the yield of the biodiesel.    DETAILED DESCRIPTION - Preparing biodiesel comprises: (i) under first near-critical reaction conditions, carrying out contact reaction of a grease raw material and monohydric alcohol to obtain a mixture containing crude fatty acid monoalkyl ester; (ii) passing the mixture containing crude fatty acid monoalkyl ester into a flash tower to carry out flash evaporation for dehydration, thus obtaining a monohydric alcohol-water gas mixture from the tower top, and passing the monohydric alcohol-water gas mixture into an alcohol recovery tower to recover the monohydric alcohol so as to obtain the monohydric alcohol from the tower top, and returning a part of recovered monohydric alcohol into the flash tower, where the quantity of the monohydric alcohol returned into the flash tower enables the water content in the dehydrated mixture obtained from the bottom of the flash tower to be not higher than 1 wt.%; and (iii) under second near-critical reaction conditions, carrying out contact reaction on the crude fatty acid monoalkyl ester in the dehydrated mixture and the monohydric alcohol.
NOVELTY - A carbonyl group-containing compound (II) and organic compound (III) are reacting in organic solvent in the presence of catalyst, and nucleophilic substitution reaction is carried out, to obtain 2-(2-methanesulfonylethyl)-2,3-dihydro-1H-isoindole-1,3-dione.    USE - Preparation of lapatinib intermediate (claimed).    ADVANTAGE - The lapatinib intermediate is efficiently prepared without polluting the environment, by a simple method.    DETAILED DESCRIPTION - A carbonyl group-containing compound of formula (II) and organic compound of formula: -(S(=O)-O-)n M (III) are reacting in organic solvent in the presence of catalyst, and nucleophilic substitution reaction is carried out, to obtain 2-(2-methanesulfonylethyl)-2,3-dihydro-1H-isoindole-1,3-dione.    X=chloro or bromo;    M=sodium, potassium or zinc;and    n=1 or 2.
NOVELTY - Method of synthesizing methane involves forming mixed gas by adding steam to synthesis gas which is formed of carbon monoxide and hydrogen, and supplying mixed gas to reactor and insulative reactor. The amounted of added steam is 10-50 volume% with respect to total volume of synthesis gas and steam.    USE - Method of synthesizing methane (claimed).    ADVANTAGE - The method efficiently provides methane from synthesis gas, by simple method by effectively controlling reaction heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for synthesizing methane.
NOVELTY - The manufacturing system has first anaerobic fermentation tub (70) that is connected to second anaerobic fermentation tub (80). The food waste in the livestock excretion is desulfurized and dried at certain temperature. The heat exchanger is supplied to the gas holder (90) through the cooling device. The gas holder is connected to boiler (120). The livestock excretion waterspout (1) and food waterspout (2) are alkalized through generator (130), so as to generate biogas.    USE - Biogas manufacturing system used in electricity facility, livestock farm facility, thermal power generation plant and village.    ADVANTAGE - The biogas can be generated effectively without causing any bad smell. The energy and cost required for generating biogas can be saved. The economic benefits of the biogas generating system can be improved. The waste can be processed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas manufacturing system. (Drawing includes non-English language text)    Livestock excretion waterspout (1)    Food waterspout (2)    First anaerobic fermentation tub (70)    Second anaerobic fermentation tub (80)    Gas holder (90)    Boiler (120)    Generator (130)
NOVELTY - Preparing 6-chloro-2-mercapto-benzoic acid comprises (a) mixing 2,6-dichloro-benzonitrile, solvent and sodium sulfide nonahydrate, vacuum extracting and distilling, carrying out thermal reaction, and recovering solvent; and (b) mixing the product obtained in the step (a) with inorganic alkali aqueous solution, conveying into a high pressure kettle, carrying out thermal reaction, placing the reaction kettle into an enamel reaction kettle, cooling frozen salt water, adjusting pH, extracting, washing, drying anhydrous sodium sulfate, concentrating, placing in a crystallizing barrel, and cooling.    USE - The method is useful for preparing 6-chloro-2-mercapto-benzoic acid (claimed).    ADVANTAGE - The method: is simple; has low production cost, high total yield and low pollution; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing 6-chloro-2-mercapto-benzoic acid comprises (a) mixing 2,6-dichloro-benzonitrile, solvent and sodium sulfide nonahydrate, vacuum extracting and distilling to remove most of the water, carrying out thermal reaction, after completing the reaction, recovering the solvent by distillation, and then directly using in the next step; and (b) mixing the product obtained in the step (a) with inorganic alkali aqueous solution, conveying into a high pressure kettle, carrying out thermal reaction, completing the reaction, placing the reaction kettle into an enamel reaction kettle, cooling frozen salt water, adjusting pH to acidic with dilute acid, then extracting the product with an organic solvent, washing with water for two times, drying anhydrous sodium sulfate, concentrating to obtain oily matter, placing in a crystallizing barrel, and cooling the condensed solid to obtain 6-chloro-2-mercapto-benzoic acid.
NOVELTY - The furnace has a furnace body whose upper part is provided with a combustion chamber and lower part is provided with a gasification chamber. The gasification chamber is connected with the combustion chamber by a guide pipe. An air hole is formed at a bottom part of the gasification chamber. A secondary air channel is connected with a guide pipe that is formed on a side wall of the air hole. An upper end of the furnace body is formed with a poly-combustion nozzle. The furnace body is connected with a main air channel by an adjusting valve.    USE - Biomass semi-gasification furnace.    ADVANTAGE - The furnace has high absorption and utilization rate, better energy-saving effect, ensures quick fire characteristic and reduces release of heat.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass semi-gasification furnace.
NOVELTY - This patent aims at high altitude, it claims a high altitude area waste water treating the solar heating system and method using inner and outer double-layer water tank, water tank for waste water, waste water is used for marsh gas fermenting it at high temperature, outer water tank for a water circulation, a heat supply. Combined with solar energy heat utilization technology, waste water treatment and biogas fermentation technology, the high altitude area hot water supply and waste water heating and marsh gas fermentation. Water tank, a snake-shaped design, it can effectively increase the heat exchange area and the waste water to obtain the high efficiency rapid heating, a system component structure can be assembled, it can be designed according to the requirement of water tank through a control valve, is provided with a waste water to the waste water fermentation according to the water temperature, and a hot water can be supplied for people life. Compared to find the current solar energy auxiliary heating marsh gas fermentation technique, the system can effectively avoid the switch tube in the conventional technique easy to be corroded, the heating is not uniform, heat loss is large.
NOVELTY - Fuel, preferably incendiary agent to cut open the tree leaves, comprises dried paraffin granules and powder which are mixed together in ratio 1:1. The mixture is pressed under the heat influence for cutting after cooling, trimming or producing pellets. The incendiary agent is provided in the fireplace of small heating installations communicating with heating systems. The fuel supplies heat to the systems around houses e.g. opened wood pellet.    USE - The incendiary substance, preferably incendiary agent is useful for generating heat and power and to cut open the tree leaves (all claimed).    ADVANTAGE - The incendiary substance: provides solid form with uniform dimensions which allows it to burns for longer time (claimed); and can be produced in simple and cost efficient manner.
NOVELTY - The binder comprises mixtures of juice extracts of cactus, taro leaves, stalks, corn stalks, banana trunks and lime stone powder.    USE - Binder for producing solid fuel that is utilized in e.g. cement factories. Uses include but are not limited to steel mills, furnace industries and thermal power plant.    ADVANTAGE - The binder prevents environmental hazard cause by slagging and fouling from the furnace industries and thermal power plant.
NOVELTY - A sorbent comprises urea formaldehyde polymer.    USE - Sorbent is used for extracting oil spills, benzene, fuel oil and other liquid hydrocarbons, and water from solid surface (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for extracting oil spills, benzene, fuel oil and other liquid hydrocarbons, and water from solid surface, which involves applying sorbent to the surface of spill.
NOVELTY - An anaerobic sludge bed reactor comprises tank, inlet water pipe (1), water distributor (2), three-phase separator (3), gas-liquid separating sloping plate, solid-liquid separating sloping plate, reactor feeding pump, weir, baffle plate and biogas collection area (12).    USE - Anaerobic sludge bed reactor for treating organic wastewater (claimed).    ADVANTAGE - The reactor is simple, small, and low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of anaerobic sludge bed reactor (Drawing includes non-English language text).    Inlet water pipe (1)    Water distributor (2)    Three-phase separator (3)    Pressure transducer interface (10)    Biogas collection area (12)    Gas nozzle (13)
NOVELTY - This utility model claims a kind of controlling sulfureted hydrogen continuously and stably preparing hydrogen by decomposing device, belonging to the hydrogen production and gas purification technology field, wherein the utility model is a hydrogen sulfide gas or gas containing hydrogen sulfide is in a spiral mode along the axial direction reverse rotational flow through the discharge area, dielectric barrier discharge high energy electron to hydrogen sulfide, passes through a discharge area so that the generated sulphur from discharging area. The utility model has advantages of under normal pressure and non-catalytic condition, a dielectric barrier discharge to realize hydrogen sulphide is high energy efficiency, decomposing hydrogen and sulphur can be away from the discharge area and decomposition reaction can be carried out continuously and stably, sulfureted hydrogen decomposition rate and high energy utilization rate. The utility model is suitable for natural gas, petroleum and coal chemical industry containing hydrogen sulphide gas dissociation hydrogen and elemental sulphur, the device has no special or limited, so that hydrogen and sulphur having general applicability for hydrogen sulfide decomposition of source and is composed of a gas.
NOVELTY - A hydrogen production apparatus comprises modification part (6) which generates reformed gas which contains hydrogen by modifying raw fuel and water vapor, mixing part which mixes raw fuel and water vapor and generates mixed fluid, feed part (5) which supplies mixed fluid to modification part, outer tube which supplies water vapor to mixing part, inner tube which protrudes in mixing part and supplies raw fuel to mixing part, and flange part (36) in which flow-hole (51) which distributes water vapor from outer tube to mixing part side is formed and is provided in edge part of inner tube.    USE - A hydrogen production apparatus for fuel cell system (claimed).    ADVANTAGE - Mixing property of raw fuel and water vapor is improved. Enlargement of apparatus is prevented.    DETAILED DESCRIPTION - A hydrogen production apparatus comprises modification part (6) which generates reformed gas which contains hydrogen by modifying raw fuel and water vapor, mixing part which mixes raw fuel and water vapor and generates mixed fluid, feed part (5) which supplies mixed fluid to modification part, outer tube which supplies water vapor to mixing part, inner tube which protrudes in mixing part and supplies raw fuel to mixing part, and flange part (36) in which flow-hole (51) which distributes water vapor from outer tube to mixing part side is formed and is provided in edge part of inner tube while projecting over the edge-part side of outer tube. An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the feed part periphery of hydrogen production apparatus. (Drawing includes non-English language text).    Feed part (5)    Modification part (6)    Burner combustion chamber (19)    Flange part (36)    Flow-hole (51)
NOVELTY - The apparatus (1) has a modification unit (6) which generates the reformed gas containing hydrogen, by carrying out steam reforming of raw fuel using a burner (10). A hollow portion (51,52) has a modification catalyst (6x) and a preset flow path (61) which circulates waste gas from burner, while the modification unit forms a hollow cylinder shape. A cylindrical specific flow path (62) circulates the waste gas in opposite direction to preset flow path inside modification catalyst.    USE - Hydrogen production apparatus e.g. fuel processing system used as hydrogen supply of domestic-use fuel cell system (claimed).    ADVANTAGE - Since the cylindrical specific flow path circulates the waste gas in opposite direction to preset flow path inside modification catalyst, the flow path of the waste gas passing through the inside of modification catalyst can be lengthened, even if the length of axial direction of modification-catalyst is changed. The modification catalyst can be heated from the wall portion side of preset and specific flow paths. Therefore the uniformity of the heat transfer to modification catalyst can be improved, and the enlargement of hydrogen production apparatus can be prevented. The uniformity of heat transfer is improved, steam reforming reaction is obtained and efficiency of modifier can fully be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production apparatus in fuel cell system. (Drawing includes non-English language text)    Hydrogen production apparatus (1)    Modification unit (6)    Modification catalyst (6x)    Burner (10)    Hollow portion (51,52)    Flow paths (61,62)
NOVELTY - A hydrogen production apparatus comprises modification part (6) which produces reformed gas containing hydrogen by carrying out steam reformation of raw fuel using burner (10), carbon monoxide (CO) reduction part (7, 8) in which CO concentration of reformed gas is reduced, waste gas flow path (P3) which is positioned on outer side of modification part and CO reduction part and circulates waste gas of burner, and steam generation part (9) which is positioned on outer side of waste gas flow path, vaporizes water with heat of waste gas, and produces steam.    USE - A hydrogen production apparatus for fuel cell system (claimed).    ADVANTAGE - CO reduction part can be heated to appropriate temperature during start of operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the main body part of the hydrogen production apparatus. (Drawing includes non-English language text).    Modification part (6)    Carbon monoxide reduction part (7, 8)    Steam generation part (9)    Burner (10)    Waste gas flow path (P3)
NOVELTY - Performing a hydrocarbon conversion or processing an output from a hydrocarbon conversion in the presence of an acidic ionic liquid using a device, comprises contacting surfaces of the device with the acidic ionic liquid made of a non-metallic material, and applying the non-metallic material on a material, which is different from the non-metallic material.    USE - The method is useful for performing a hydrocarbon conversion or processing an output from a hydrocarbon conversion in the presence of an acidic ionic liquid, where the hydrocarbon conversion comprises an alkylation, a polymerization, a dimerization, an oligomerization, an acylation, a metathesis, a polymerization, a copolymerization, an isomerization, and/or a carbonylation, preferably an isomerization of methyl cyclopentane to cyclohexane (all claimed).    ADVANTAGE - The method is capable of economically, easily and stably performing the hydrocarbon conversion or processing the output from the hydrocarbon conversion in the presence of the acidic ionic liquid with high corrosion resistance.
NOVELTY - An electrolytic cell consists of an anode and a cathode of cylindrical shape, arranged coaxially and fastened at the top and bottom of Teflon (RTM: polytetrafluoroethylene) portions. The anode is a conductive nickel-coated tube with a glassy carbon, and the cathode is made of stainless steel with a nickel coating.    USE - Electrolytic cell used for producing hydrogen and oxygen-ozone mixture.
NOVELTY - The utility model claims a kind of a vehicle or a power device, especially relates to a kind of oxygen mixed power device, comprising a air inlet branch pipe of the engine, further comprising: a container is provided with an air inlet and an air outlet, the filtering liquid of the container and submerged ventilating plate in the filter liquid is composed of the filter, the air inlet is located under the liquid level of filter liquid, the air outlet is located on the liquid surface of the filtering liquid, and is connected with the air inlet branch pipe, composed of an electrolyte in the positive and negative electrode of electrolysis and electrolytic cell of a cracking tank, used to produce hydrogen and oxygen gas, and is connected with the air inlet, and the positive and negative electrolysis electrode is electrically connected with the automatic controller, used for controlling the generated hydrogen and oxygen flow rate of the inert gas, and a vehicle power is connected with the automatic controller are electrically connected. The utility model saves the fuel oil, and is more environment-friendly. And to ensure the hydrogen and oxygen gas purity, prevent hydrogen and oxygen annealing.
NOVELTY - Preparation of biodiesel oil involves crushing oil plant, sieving, then drying, placing in the extracting cylinder, adding oil extracting solvent and ester exchange solvent in double-liquid phase mixed solvent for reflowing and extracting, continuing to react, providing reaction solution color and brown yellow in the weight ratio of 1:5-15, stopping reaction, collecting, obtaining crude product, standing obtained crude product to divide into layers, separating and collecting lower layer solution, providing the collected upper layer solution as solvent and recycling.    USE - Preparation of biodiesel oil (claimed).    ADVANTAGE - The biodiesel oil is efficiently prepared with high efficiency and yield.    DETAILED DESCRIPTION - Preparation of biodiesel oil involves crushing oil plant, sieving, then drying, placing in the extracting cylinder, adding oil extracting solvent and ester exchange solvent in double-liquid phase mixed solvent for reflowing and extracting, carrying out the ester exchange reaction, adding alkaline catalyst under the condition of oil extracting solvent and oil ester exchange solvent in the weight ratio of 10-20:1, adding extracting reaction to the reaction solution in the weight ratio of 2-5:30, adding and mixing oil extracting solvent and double-liquid phase mixed solvent to the reaction solution, continuing to react, providing reaction solution color and brown yellow in the weight ratio of 1:5-15, stopping reaction, collecting, obtaining crude product, standing obtained crude product to divide into layers, separating and collecting lower layer solution, providing the collected upper layer solution as solvent and recycling.
NOVELTY - Preparing a saline modifying agent, comprises (1) drying carbon black, black powder or granular powder, (2) formulating Bacillus subtilis and Sphingobacterium multivorum, (3) drying biogas residue, crushing through 10 meshes sieve and then adding carbon black, urea and the oil-degrading bacteria complex, and (4) granulating the mixture obtained in the step (3) using circle-throw vibrating machine for 2 times, to generate columnar particles, and cooling in a cooler filter shaker and after weighing, bagging the product.    USE - The process is useful for preparing a saline modifying agent, which is useful for repairing petroleum-heavy metal composite polluted soil (claimed).    ADVANTAGE - The saline modifying agent efficiently and safely repairs petroleum-heavy metal composite polluted soil in an economical manner.    DETAILED DESCRIPTION - Preparing a saline modifying agent, comprises (1) drying carbon black, black powder or granular powder, (2) formulating Bacillus subtilis and Sphingobacterium multivorum in a ratio of 1:1 into 8x 1010 cells/ml of composite strain to form oil-degrading bacteria complex, (3) drying biogas residue, crushing through 10 meshes sieve and then adding carbon black, urea and the oil-degrading bacteria complex, where the percentage weight ratio of biogas:carbon black:urea is 88:10:2, and biogas with a total weight of carbon black and urea:high oil degradation amount of bacteria is 1 kg:1 ml, and (4) granulating the mixture obtained in the step (3) using circle-throw vibrating machine for 2 times, to generate columnar particles, where each time of granulating water is added for 3 times for 5 seconds, and cooling in a cooler filter shaker and after weighing, bagging the product.
NOVELTY - Biobased methanol fuel oil component comprises pH stable component 5C n-alkanes, 7C n-alkanes stable liquid component, 4C fatty acid ester stable viscosity component, improved cold boot component, Cn fatty ethers and 2-3C aliphatic alcohol, distillation range adjustment components Cn alkanes, and combustion stability 16-18C yeast fatty acid oil component comprising fatty acid and triethanolamine in a volume ratio of 2:1.    USE - Used as biobased methanol fuel oil component.    ADVANTAGE - The oil component can be easily prepared with good stability and is convenient to use.    DETAILED DESCRIPTION - Biobased methanol fuel oil component comprises 35 vol.% of pH stable component 5C n-alkanes, 35 vol.% of 7C n-alkanes stable liquid component, 5 vol.% of 4C fatty acid ester stable viscosity component, 41-45 vol.% of improved cold boot component, Cn fatty ethers and 2-3C aliphatic alcohol, 39-41 vol.% of distillation range adjustment components Cn alkanes, and 35 vol.% of combustion stability 16-18C yeast fatty acid oil component comprising fatty acid and triethanolamine in a volume ratio of 2:1, where the yeast EAM-AC16 is extracted by conventional fermentation under the accession number China General Microbiological Culture Collection NO.7429. The Cn fatty ether is a mixture of 30 vol.% of petroleum ether and 15 vol.% of diisopropyl ether. The aliphatic alcohol is a mixture of 6 vol.% of ethanol and 4 vol.% of isopropanol. An INDEPENDENT CLAIM is included for preparing the oil component, comprising mixing all the raw materials in a stirring kettle and then boiling, and uniformly stirring to obtain a transparent or clear, pale yellow biobased methanol fuel oil component under normal temperature.
NOVELTY - Activating agent comprises raw materials comprising 6-8 pts. wt. potassium sulfate, 12-14 pts. wt. ammonium chloride, 22-26 pts. wt. sodium acetate, 6-8 pts. wt. dipotassium phosphate, 5-7 pts. wt. dihydrogen phosphate, 2-4 pts. wt. ferrous sulfate, 20-24 pts. wt. yeast extract, 21-25 pts. wt. starch, 0.2-0.5 pts. wt. photosynthetic bacteria and 0.2-0.5 pts. wt. Bacillus subtilis.    USE - The activating agent is useful for generating methane (claimed).    ADVANTAGE - The agent enables to increase methane gas by 200-300%, and provides activation effect of 80-90% for period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of the activating agent, which involves directly adding the agent into water, dissolving mixture, and adding mixture into mixing tank.
NOVELTY - Method for making fuel, involves converting biomass from culture primarily comprising 1C metabolizing non-photosynthetic microorganism into an oil composition and refining the oil composition into fuel.    USE - The method is useful for making fuel chosen from jet fuel, diesel fuel, paraffinic kerosene and gasoline (claimed), preferably biofuels or bioplastics.    ADVANTAGE - The method enables efficient production of the biofuels in a cost-effective manner without taxing environment or competing with food production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an oil composition of 1C metabolizing non-photosynthetic microorganism, comprising molecules having hydrogen and carbon atoms, where amount of the hydrogen and carbon atoms in the molecules is at least 50% with respect to weight of the composition and content of delta 13C in the composition is -70% to -30%;    (2) recombinant 1C metabolizing non-photosynthetic microorganism capable of accumulating an increased level of fatty acids or over-expressing fatty acids when compared to parent or reference 1C metabolizing non-photosynthetic microorganism; and    (3) a 1C metabolizing non-photosynthetic microorganism biomass, where delta 13C of the biomass is -30% or less.
NOVELTY - The system (100) has a heat exchanger that is used for cooling first portion of second overhead stream prior to entering a first fractionating column through heat exchange with third bottoms stream and third overhead stream. An expander is used for expanding a portion of the second portion of second overhead stream prior to feeding the second fractionating column. A compressor is used for compressing the fourth overhead stream to produce a high pressure methane product stream.    USE - System for removing nitrogen from feed stream such as nitrogen rejection unit (NRU) feed stream and gas subcooled/expander process (GSP) feed stream.    ADVANTAGE - The nitrogen content of the sales gas can be reduced to levels that are acceptable for pipeline transport at a capital cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for removing nitrogen and producing high pressure methane product stream; and    (2) a system for removing excess nitrogen from intermediate stream in known gas subcooled process system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for removing nitrogen from feed stream.    System for removing nitrogen from feed stream (100)    GSP sub-cooler (126)    Demethanizer (140)    Expander (224)    NRU system (300)
NOVELTY - This utility model claims a kind of outer circulation anaerobic reactor, belonging to the field of sewage treatment device field, mainly composed of a shell, a water inlet port, marsh gas inlet, mixing chamber, a reaction chamber, a separating chamber, a biogas, a rotational flow water distributor, separating module, a circulating system, wherein the housing is a closed cylindrical tank body, the bottom is provided with a water inlet, and the top is provided with gas outlet, the mixing chamber is set at the bottom of the shell body, the upper part of the mixing chamber is provided with a reaction chamber, the reaction chamber is set on the upper part of the separation chamber, separating chamber is provided with a separating module, a marsh gas chamber is set on the upper part of the separating chamber, an outer circulation system is arranged on the external part of one side of the shell. This utility model is a mixed effect of mixing chamber, stirring intensity, separating stirring intensity and mass transfer effect of deposition function, a reactor chamber are provided with reinforced, which effectively prevents the loss of the anaerobic sludge, improves the processing efficiency and the volume load of the reactor, expands the application range, reduces the occupied area of the reactor.
NOVELTY - Vehicle load straw processing system, belonging to the field of environmental protection equipment technology field, comprising a feeding device, a carbonization device, tar extracting device and gas extracting device on the vehicle body integrated carbonization furnace, the biomass combustible gas compression and cooling, collecting and storing, solid carbon and as a whole, of the vehicle body in the vehicle and can move, and matched with vehicle straw fuel processing system is configured including electric power, such as a different energy, it is convenient to use, the utility model is new-type on-vehicle straw processing system for a process, there is no three wastes generated, all capable of efficient resources;
NOVELTY - The utility model claims an intermittent biomass pyrolysis carbon production device, belonging to the field of biomass pyrolysis. This utility model is composed of a heating furnace body, axe, heating furnace is fire-resisting layer, a shell and a smoke discharging hole, hole is connected with a draught fan by a pipeline to the combustion chamber, dry distillation axe is set in the thermocouple, a axe is provided with a combustion chamber, a movable cover board, a movable cover plate is provided with a fuel gas exhaust pipeline, dry distillation axe the ends of the annular surface of the movable cover plate is high temperature resistant sealing ring, so it can effectively prevent the inner and outer air enter into dry distillation axe, high leak tightness, on the other hand avoids the gas leakage, the utility model beneficial effects are as the biomass into carbon, generating a plurality of additional product, which overcomes the straw directly used as fuel energy utilization rate is low, the use is limited, the environment pollution and so on.
NOVELTY - This utility model claims a kind of suitable for a carbon of biomass for rural village or household is a unit such as straw, comprising a carbide furnace, barrel (8) and the moving and rotating auxiliary component, oil gas burning element. Carbonization is composed of combustion chamber (11), the cavity (4, 2), a return channel (21), a guide rail (5) and a sealing door (10, 13), a furnace body with 5-10 degrees. Dry distillation barrel is composed of a barrel body, oil outlet and rotating shaft. Guide rail (5) is fixed on the furnace wall of carbonization furnace (1) on the base (23). A guide rail running guide rail (6), and a parallel guide rail is a metal rod. A dry distillation barrel hung car guide rail, and the rotating of the transmission rod through the furnace wall (19). A dry distillation barrel cracking oil gas is connected with the air outlet of a U-shaped tube (9) guided to carbonization barrel, the combustion chamber the hot air for combusting and heating dry distillation barrel, a carbon source and avoids the air pollution.
NOVELTY - The utility model claims a hydrogen-oxygen mixed power device, especially a hydrogen and oxygen generator of the device. Comprising: a multiple connection of the electrolytic cell, of the electrolyte in the electrolytic bath and placed in the electrolyte of the electrolytic electrode is composed of a cracking tank, the electrolytic solution contains alcohol, ethylene glycol, organic silicon de-foaming agent and alkali, the electrolytic electrode is plated on the surface of a layer of alloy of nickel-base stainless steel alloy is nickel sulphur, nickel, nickel chromium, nickel iridium alloy, and is electrically connected with the automatic controller of the electrodes for electrolysis, which is used for controlling to produce hydrogen, the flow rate of the oxygen gas. This utility model is electrolytic electrode and the electrolyte to react under the control of the automatic control so that the hydrogen-oxygen mixed gas is continuously on the electrolysis electrode, and is transmitted to the engine.
NOVELTY - A kind of gas-water circulating system, which is applied to generate a hydrogen-oxygen in the electrolytic water. A gas circulating system comprises an electrolytic groove, is provided with a first air outlet, adapted to receive an electrolytic water on the upper part of the electrolytic cell, and a first water inlet, wherein the electrolytic groove, and the electrolytic water electrolysis to produce hydrogen and oxygen. A gas circulation system further comprises a first water storage barrel and is suitable for containing pure water. The first water storage barrel comprises a gas inlet is configured on the lower part of the first water storage barrel, a gas inlet and outlet of the electrolytic cell is coupled, a first water outlet, a water outlet port coupled to the first water inlet, a second gas outlet, is arranged on the upper part of the first water storage tank, and a pressure releasing device configured on the upper part of the first water tank. A time exceeds a preset pressure when the hydrogen and oxygen in the first water storage barrel so as to be suitable for pressure relief through the pressure relief device. This utility model is applied to the electrolytic bath for health care gas generating hydrogen and oxygen, capable of hydrogen and oxygen in a system so as to prevent hydrogen decrepitation.
NOVELTY - Installation comprises bioreactor with heater, hermetic container of cylindrical form, system for supply of preliminarily heated and ground initial feedstock, system for intensive mixing of biomass, system for removal of biogas from the reactor, vacuum pump, control system, system for unloading and bottling finished product, system for preliminary heating of initial feedstock made in form of coil, container for preliminary heating and mixing of feedstock and mating with the bioreactor.    USE - The installation is useful for anaerobic processing of organic wastes of phytogenic or plant origin, and production of biogas and liquid organic fertilizer (claimed).
NOVELTY - Firelighters i.e. igniting blocks produced from a pressed and dried green waste, for lighting small combustion plant having a thin brick size, is claimed.    USE - The firelighters are useful for lighting small combustion plant having a thin brick size (claimed).
NOVELTY - A biological diesel oil is processed by carrying out transesterification reaction of grease with presence of catalyst which is sodium hydroxide at 150-155 degrees C temperature and 0.8-0.85 MPa pressure to obtain a homogenous reaction system.    USE - Reaction process of biological diesel oil (claimed).    ADVANTAGE - The reaction process has short reaction time and high conversion rate.
NOVELTY - This utility model belongs to a kind of water electrolysis oxygen device, wherein it is as follows: oxygen-hydrogen generator, wherein is formed by air chamber plate, electrode plate, the electrode plate and an end cover, wherein the assembling pole, electrolyte tank and each gas cell plate are connected by a single connecting pipe, a liquid inlet hole enter into hydrogen and oxygen chamber, the base is set with a groove are respectively matched with the electrolyte box and oxygen hydrogen generator, is adhered by adhesive. The oxygen generator is simple in structure, accurate and convenient, the sealing is good, and it is safe and reliable, oxygen purity is high, which can reach more than 99%, it can be made into large and a kind of the type is suitable for family, hospital, vehicle and ship, meeting room and movable;
NOVELTY - The utility model claims a hydrogen-oxygen generating vehicle electrolytic cell, comprising an electrolytic cell main body, wherein the electrolytic cell main body is provided with a side by side a plurality of electrode plate separating the not more than 10 in series with each other between the electrolysis chamber, the adjacent electrode plate clamp is provided with electrolytic chamber for sealing edge of the sealing frame are respectively provided with electric pole is connected with the outermost end of the two electrode plates on the outermost end of the any one of the electrode plate is provided with electrolytic chamber electrolyte inlet and gas outlet. This utility model is electrolysis chamber is not more than 10, so the whole electrolytic groove has thin thickness, it occupies small space, it can be directly mounted on the engine near the head, which greatly improves the convenience of installation, and is easy to improve the heat efficiency of the electrolytic cell. This utility model also claims a generating system for combustion-supporting of a vehicle with hydrogen. This utility model is suitable for the technical field of automobile.
NOVELTY - A methane fermentation system (1) comprises methane fermentation equipment (2) which carries out methane fermentation treatment of organic waste water, and saturated oxygen liquid introduction unit (10) which introduces saturated oxygen liquid into methane fermentation equipment which has acid production part and methane fermentation part of microaerobic property by oxygen.    USE - A system for fermenting methane (claimed).    ADVANTAGE - Hydrogen-sulfide inhibition is stably suppressed without inhibiting production of methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane fermentation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the methane fermentation system. (Drawing includes non-English language text).    Methane fermentation system (1)    Methane fermentation equipment (2)    1st flow volume controller (3a)    Saturated oxygen bath (4)    Saturated oxygen liquid introduction unit (10)
NOVELTY - A system for harvesting algae, comprises: a mechanical harvesting system, and a chemical harvesting system.    USE - As system useful for harvesting and processing algae, to produce biodiesel, biosolvents, bioplastics, biogas or fertilizer (claimed).    ADVANTAGE - The present system is flexible enough to provide for an economically viability and commercially feasible system of processing biomass, particularly algae.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a system for harvesting and processing algae, comprising: a rotating bioreactor harvester, a chemical harvesting module, a biodiesel producing module, a biosolvent producing module, a bioplastics producing module, and a biogas and fertilizer producing module; and    (2) method for harvesting and processing algae, involving: harvesting algae, and processing algae.
NOVELTY - Inactivating the microbial host cell in a fermentation broth comprising an enzyme of interest and the microbial host cell producing the enzyme of interest comprises: (a) adding a fatty acid having a chain length of 4-12C to the fermentation broth; and (b) mixing the fermentation broth for a sufficient period of time until the microbial host cell is inactivated.    USE - The method is useful for inactivating the microbial host cell in a fermentation broth comprising an enzyme of interest and the microbial host cell (claimed); and for industrial applications where a crude enzyme solution may be adequate, e.g., in bio-ethanol applications (e.g. biomass conversion).    ADVANTAGE - The method produces desired enzymes as a crude product in industrial scale.
NOVELTY - Preparation of nafamostat mesylate involves preparing anion-exchange resin in which anion is mesylic acid ion, contacting anion-exchange resin with nafamostat salt chosen from neither nafamostat bicarbonate and other salt excluding nafamostat mesylate, in presence of solvent to convert nafamostat salt into nafamostat mesylate by salt-exchange, and crystallizing obtained salt.    USE - Preparation of nafamostat mesylate used for treating pancreas disease e.g. pancreatitis, disseminated intravascular coagulation, and bleeding lesions, and preventing coagulation of perfusion blood during blood extracorporeal circulation of patients with bleeding tendency (claimed).    ADVANTAGE - The method efficiently and economically provides nafamostat mesylate, without causing pollution to environment.
NOVELTY - This invention relates to a hydrogen generation system and more particularly to a hydrogen fuel power generation system with energy conservation and carbon reduction effects, comprising a battery module, an oxyhydrogen generation module, a pressurization module, an internal combustion machine module, a transmission module, a power generation module, and a control module. A pressure detector is disposed between the oxyhydrogen generation module and the control module, a pressure detector is disposed between the pressurization module and the control module, and a gas intake mixer connected to the control module is disposed between the pressurization module and the internal combustion machine module. Therefore, hydrogen and oxygen can be stably injected into the internal combustion machine module, and the operation of the internal combustion machine module can drive the transmission device to further drive the power generator for converting kinetic energy into electrical energy which can be used by electrical appliances and synchronously for feedback on the battery charging for repeated operation of the oxyhydrogen generation module and achieving the purposes of energy conservation and carbon reduction.
NOVELTY - Oxygen carrier comprises perovskite complex metal oxide of ABO3, where A is alkaline earth metal barium, B is transition metal nickel, iron, or cobalt.    USE - Used as an oxygen carrier.    ADVANTAGE - The oxygen carrier is economical, has high cyclic activity, and has good high temperature stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the use of oxygen carrier in preparing hydrogen by chemical looping, where the reaction temperature of oxygen carrier in fuel and steam are respectively 600-1200 degrees C, and the reaction pressure is normal pressure, and in chemical looping combustion techniques, where the air combustion temperature is 400-1000 degrees C, and combustion temperature after fuel reduction is 400-1000 degrees C, and the reaction pressure is normal pressure; and    (2) preparing oxygen carrier by co-precipitation method, specifically comprising using nickel nitrate, ferric nitrate, cobalt nitrate and barium nitrate as the precursor, where the number of moles of nickel ion, ferric ion, and cobalt ion is equal to the number of moles of calcium ions, mixing and stirring uniformly to prepare solution, using aqueous ammonia as precipitator for co-precipitation reaction, controlling the pH value at 8-12 (preferably 9-11), after precipitating completely, aging, filtering, washing, drying and calcining to obtain the perovskite metal oxide oxygen carrier.
NOVELTY - Absorbent solution comprises water, and alkylamino piperazines, preferably 1-methyl-4-(3-dimethylaminopropyl)-piperazine and 1-ethyl-4-(diethylaminoethyl)-piperazine.    USE - The absorbent solution is useful for removing acid compounds contained in a gaseous effluent such as natural gas, synthesis gas, combustion fumes, refinery gas, acidic gas obtained from an amine unit, Claus process tail gas obtained from a reduction unit, biomass fermentation gas, cement gas and incinerator fumes or removing hydrogen sulfide from gaseous effluent comprising carbon dioxide (all claimed).    ADVANTAGE - The absorbent solution enables energy-efficient removal of acid compounds contained in the gaseous effluent in an environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removing acid compounds contained in gaseous effluent, comprising absorbing acid compounds using the absorbent solution.
NOVELTY - A homopiperazine is prepared by (1) reacting ethylenediamine and amino protecting agent and water with mol ratio of 1:2-6 to obtain N,N'-1,4-di-Boc-ethylenediamine in which mass ratio ethylenediamine:water is 1:0.8-1.2, (2) mixing with 1,3-dihalopropane and sodium alkoxide in alcohol mole ratio of 1:1-1.5:3, performing cyclization reaction to obtain N,N'-1,4-di-Boc-homopiperazine, (3) deprotecting with halogenated hydrocarbon solution of alcohol under saturated solution to obtain hydrogen halide homopiperazine, adjusting pH with alkali, and extracting with ethyl acetate.    USE - Preparation of homopiperazine (claimed).    ADVANTAGE - Product is low-cost, and has easy to obtain raw material, high yield, and less pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a proton nuclear magnetic resonance spectrum of homopiperazine.
NOVELTY - An ammonia filter tip interception determination method involves establishing standard working curve by utilizing ammonia ion standard solution, taking hydrochloric acid as solvent, and preparing ammonia ion series standard work solution with different concentrations, taking sample in conical flask, adding hydrochloric acid, shaking mixture, taking extraction solution, filtering mixture, analyzing through ion chromatography analysis, and setting ion chromatography detection condition by selecting mixture of methane and water as mobile phase and controlling 1.2 ml/minute as flow speed.    USE - Method for determining ammonia filter tip interception in mainstream smoke.    ADVANTAGE - The method enables determining ammonia filter tip interception with high repeatability and recovery rate.    DETAILED DESCRIPTION - An ammonia filter tip interception determination method involves establishing standard working curve by utilizing 1000 mu g/ml ammonia ion standard solution, taking hydrochloric acid as solvent, and preparing ammonia ion series standard work solution with concentrations of 1.0 mu g/ml, 0.8 mu g/ml, 0.4 mu g/ml and 0.2 mu g/ml, taking sample in conical flask, accurately adding 100 ml hydrochloric acid, shaking mixture for 40 minutes, standing for 5 minutes, taking 2 ml extraction solution, filtering mixture through 0.45-micron filter membrane, purifying filtrate, analyzing through ion chromatography analysis, and setting ion chromatography detection condition by selecting mixture of methane and water as mobile phase and controlling 1.2 ml/minute as flow speed.
NOVELTY - A core-shell structure composite membrane catalyst comprises shell having a layer of molecular sieve and porous aluminum oxide or molecular sieve and silicon oxide composite film. The composite film has thickness of 2-30 mu m.    USE - Core-shell structure composite membrane catalyst used in carbon dioxide hydrogenation to prepare low-carbon hydrocarbon (claimed).    ADVANTAGE - The catalyst can effectively realize continuous coupling reaction in the same reactor and has mild reaction preparation condition which does not affect the active core of the catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon dioxide hydrogenation to prepare low-carbon hydrocarbons, comprising adding composite film core-shell structure catalyst into a reaction vessel, supplying mixed gas comprising hydrogen and nitrogen, where hydrogen content of mixed gas is controlled to 5 vol.%, heating the reaction vessel from room temperature to 200-500 degrees C at 1-10 MPa, and reacting with raw material gas comprising hydrogen and carbon dioxide at volume ratio of (1-6:1).
NOVELTY - A biological fuel oil contains 5-85 wt.% palm oil, 5-55 wt.% benzene, 5-65 wt.% methylal, 5-85 wt.% methanol, 1-15 wt.% oleic acid, 0.05-5 wt.% Span 80 (RTM: Sorbitan monooleate), 3-35 wt.% methyl acetate, 0.05-10 wt.% potassium permanganate, and 0.01-5 wt.% dicyclopentadienyl iron.    USE - Biological fuel oil for boiler (claimed).    ADVANTAGE - The biological fuel oil is environment-friendly, has high heat value, easy ignition, strong fire power, low corrosion to combustion device, and low viscosity, does not need pre-heating, prolongs boiler service life, and improves burning efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological fuel oil which involves pre-heating palm oil at 60-90 degrees C, melting, pumping in stirring tank at normal temperature and pressure, starting stirrer, adding benzene, methylal, and methanol sequentially, continuously stirring for 10 minutes, adding oleic acid, Span 80 (RTM: Sorbitan monooleate), and methyl acetate sequentially, continuously stirring for 10 minutes, adding potassium permanganate and dicyclopentadienyl iron sequentially, continuously stirring for 10 minutes, uniformly mixing in heated static mixer for 30 minutes, standing for 30 minutes, and filtering.
NOVELTY - Biomass pyrolysis and liquefaction with explosion-proof ash discharging system, belonging to the technical field of renewable energy sources and it is as follows: it comprises a feeding port, a material conveying tube and a sand box, a feed port is set on the conveying tube, the conveying material cylinder and the sand box, the sand box is provided with sand, and the height of the sand is higher than conveying material cylinder is provided with turning roller and the connecting part of the sand box, the sand box, the sand box is provided with air suction cover. This utility model uses sand capable of obtaining good sealing effect, and it can realize biological carbon ash is continuous, set with a explosion protection personnel and device safety.
NOVELTY - A blade type biomass thermal cracking reactor, belonging to the technical field of renewable sources utilization, comprising a shell, wherein the upper part of the shell is equipped with a biomass feeding port, lower part of the shell is provided with a cleaning port pyrolytic carbon and pyrolysis gas product outlet, the shell is provided with a rotating shaft, the rotating shaft is provided with a plurality of rotating vanes, the outer shell is covered heat insulating layer. This utility model lifting temperature quickly, high heat efficiency, biomass material friction, rolling in the reactor, it can fully contact, fully.
NOVELTY - This utility model claims a kind of single captured organisms is a compound condensation collecting device, belonging to the biomass resource and energy technology field. Comprising: a biomass pyrolysis steam condensate is sleeve type condenser for collecting the condensed to obtain the bio-oil of the oil storage tank of the first stage for the high-voltage electric field, the primary pyrolysis gas of the oil phase component enriched generating biological oil and pyrolysis gas is set with condensing of the collector for collecting biological oil of the oil storage tank for providing the direct current high voltage of the high-voltage generator with electric collector for condensing cover for circulating bath groove circulating heat dissipation of condensing medium for secondary pyrolysis gas capture by a filtering and purifying to collect the filter of the bio-oil, used for collecting three-grade oil third level biological oil. The device is simple in structure, low in cost, convenient to operate and a biological oil collecting efficiency is high.
NOVELTY - A kind of high automatic continuous biomass pyrolysis oil on-line separation and quick cooling system, comprising a storage tank, a solid-liquid separation, a buffer tank, a condenser and oil outlet pipeline of the oil storage tank is connected with a solid-liquid separation, solid-liquid separation of a liquid phase pipeline is connected with the buffer tank, a discharging pipeline of the buffer tank are connected with the condenser and the storage tank, the discharge pipeline of the buffer tank is provided with a reflowing pipeline is connected with a oil storage tank outlet pipeline, the buffer tank is provided with the online sampling detection device. This utility model can carry out heat separating the pyrolysis oil and improves the oil quality and to avoid the heat solve a coking caused by blockage of the pyrolysis oil rapid cooling, it can effectively reduce cracking oil component in the polymerization reaction, to obtain low-viscosity oil, stored for a long time the viscosity increasing rate.
NOVELTY - This utility model claims a down suction type garbage treatment gasification furnace, comprising a furnace body, a stirrer, a furnace body with a furnace body bottom is divided into drying section, a pyrolysis section, burning section and reducing section, wherein the stirrer is installed on the drying area, the upper part of the furnace wall of the combustion area is provided with the air pipe, and further equipped with a thermoelectric couple in the furnace wall of the combustion area, the utility model comprising a gas and organic material to flow downwards through the high temperature area, the gasification reaction, wherein the gas-solid in order to flow the gas tar content gasification furnace generate less, on one hand it can simplify subsequent processing device, on the other hand can effectively reduce the secondary pollution to the environment. Garbage for certain components of small density, flow property is bad, easy to bridge, pumping and so on, device suitable stirrer, the material smoothly move downwards to realize the uniform and stable gasification furnace operation.
NOVELTY - This utility model claims a kind of mulberry as raw material for charcoal production device, belonging to the technical field of machinery. It solves the problem that the existing machine-made charcoal production device has low automation degree, low production efficiency and so on. A kind of mulberry as raw material for charcoal production equipment, the production equipment comprising a crusher, a drier, a making and carbonizing furnace, to the first feeding machine and a drying machine and the crushed raw material, the raw material after drying according to a second machine to machine, machine and the second feeding machine is provided with a dosing machine, making the furnace. The utility model is provided with high automation degree, high production efficiency and so on.
NOVELTY - This utility model claims a straw carbonizing furnace waste gas recycling device, wherein is suitable for straw carbonizing furnace manufacturing straw charcoal process on straw raw material rod to generate the carbon monoxide recycling device. A exhaust pipe, a gas collecting pipe, an air storage cabinet, a draught fan and a gas pipe, a plurality of exhaust pipe and the straw carbonization furnace exhaust is connected with the several exhaust pipe is connected with the gas collecting pipe, a draught fan air inlet is connected with the gas collecting pipe, a draught fan outlet is connected with the air storage tank, an air storage cabinet through the gas pipe is connected with . Set provided with a valve on the gas pipe. Straw carbonization furnace waste gas recycling device has reasonable design, compact structure, wherein the straw carbonizing furnace of straw carbon raw material rod generated in the process of large amount of carbon monoxide gas to a gas storage cabinet by the draught fan to the use point, a drier, a gas furnace, a burning furnace air supply pipe, an ignition combustion, makes full use of the energy, reduce the environmental pollution and achieve the purpose of low carbon energy-saving discharge through the transporting pipeline.
NOVELTY - This utility model claims a kind of new-type full automatic adjustment of low tar-free straw gasification device, comprising a gasification furnace body, the lower part of the gasification furnace body is provided with fire grate, the fire grate is provided with a rotating shaft and a center rotating shaft passes through the ash with the speed reducer is connected with the inner box is provided with a water flushing pipe and a discharging pipe, the angle of the water flushing pipe and discharging pipe is 180 degrees. The fire grate is a grate. The speed reducer is connected with the controller. The beneficial effect of the utility model is: straw through a high strength of the combustion air and the necking variable diameter in the gasified tar generated by high temperature cracking, fire grate uses a fire grate, the lower the speed reducer drive, a fire grate rotating process of the automatic ash-removing, gasification agent into the necking variable-diameter section to realize the electric coupling between the forced area, so as to generate high temperature by air, generated during the thermal cracking of tar by high temperature area, can be cracked, so as to remove tar.
NOVELTY - This utility model claims a biomass gasification furnace combustible gas cooling device, comprising a gasification furnace is connected with a spiral dust remover (13), a spiral dust remover (13) is connected with the air pipe (5), a primary cooling mechanism, air delivery pipe (9) is connected with the secondary cooling, wherein the secondary cooling mechanism comprises a water tank (6), a water tank (8), a water tank (6) is provided with an air inlet, an air outlet (2), a U-shaped tube (3) and the clapboard (4), an air inlet pipe (9) is connected with the gas in the upper part of the water tank (6) is U-shaped pipe (3), a clapboard (4) is connected with the lower water tank (8) is composed of at least 2 cooling chamber (7), a combustible gas through a gas pipe (9) enters into the upper part of the water tank (6), the cooling chamber (7), a U-shaped tube (3) is cooled by the air outlet (2), the utility model is a combustion gas temperature is reduced to 20 degrees centigrade, cooling, the purifying effect is good, the combustible gas can be purified to more than 98%, but also can realize recycling the tar, vinegar liquid.
NOVELTY - Alkali-refining vegetable oil-refining byproduct-soap and acid are mixed, acidified and separated. Acidified oil and crude glycerol are added, esterified under alkali catalyst (A), to obtain esterified oil. The esterified oil and methanol are added and ester exchange reaction is carried out under alkali catalyst (B) to obtain fatty acid methyl ester and crude glycerol. Fatty acid methyl ester is recycled and biodiesel is obtained. Biodiesel is directly used as fuel for deodorizing process. The obtained acidic wastewater and alkaline water are mixed, separated, acidified and recycled.    USE - Recycling of alkali-refining vegetable oil-refining byproduct-soap (claimed).    ADVANTAGE - The recycling of alkali-refining vegetable oil-refining byproduct-soap is economically enabled without affecting environment.    DETAILED DESCRIPTION - Alkali-refining vegetable oil-refining byproduct-soap and acid are mixed in mass ratio of 0.1-2:1, acidification is carried out, and acidified oil layer as upper layer and aqueous layer as lower layer are separated. Acidified oil and crude glycerol are added in mass ratio of 0.2-0.6:1, esterification reaction is carried out under alkali catalyst (A), to obtain esterified oil. The esterified oil and methanol are added in mass ratio of 0.2-0.4:1, and ester exchange reaction is carried out under alkali catalyst (B) to obtain the fatty acid methyl ester and crude glycerol. Fatty acid methyl ester is recycled and biodiesel is obtained. The biodiesel is directly used as fuel for deodorizing process. The obtained acidic wastewater and alkaline water are mixed in mass ratio of 1:0.5-5, separated, acidified and acidified oil is directly used for biodiesel and aqueous layer is discharged. An INDEPENDENT CLAIM is included for soap-stock acidification reactor.
NOVELTY - This utility model claims a method for extracting and purifying methane and carbon dioxide from marsh gas impurity, comprising a cooling device, a separate, methane gas, carbon dioxide gas and pipeline inlet valve is set at the front end and the rear end is provided with an outlet valve and a vacuum pressure gauge, a separate cooling device is placed in the separation chamber is further equipped with a heating device, a separation chamber is connected with the third air valve is set between the air outlet pipe section, a separation chamber with the pipeline between the inlet valve and the outlet valve of the pipeline, methane gas bottle is connected with a methane bottle feeding pipe is provided with a first air valve is set on the methane bottle feeding pipeline, a gas cylinder is connected with a carbon dioxide feeding pipe is provided with a second air valve is set on the carbon dioxide feeding pipe, the bottom of the methane bottle connected with the separating chamber is connected with the top of the carbon dioxide feeding pipe and the separating chamber on the upper part corresponding to the pipeline are respectively provided with a pressure meter. The utility model passes through the structure, it can improve the marsh gas component accumulation rate can be extracted with high purity.
NOVELTY - A biodiesel catalyst comprises calcium (Ca), magnesium (Mg), zinc (Zn), aluminum (Al), and oxygen (O) at specified molar ratio.    USE - Biodiesel catalyst.    DETAILED DESCRIPTION - A biodiesel catalyst comprises Ca, Mg, Zn, Al, and O (n(Ca):n(Mg):n(Zn):n(Al):n(O)) at specified molar ratio of 0.3-0.7:2:0.3-0.7:1:4.1-4.9. An INDEPENDENT CLAIM is included for preparation of catalyst by (A) mixing 0.3-0.7 pts. wt. calcium nitrate tetrahydrate, 2 pts. wt. magnesium nitrate hexahydrate, 0.3-0.7 pts. wt. zinc nitrate hexahydrate, 1 pt. wt. aluminum nitrate nonahydrate at molar ratio of 0.3-0.7:2:0.3-0.7:1:6:3 to obtain first solution; and mixing sodium hydroxide and 3 pts. wt. sodium carbonate to obtain second solution; (B) mixing two solutions to carry out coprecipitation reaction, aging, filtering, washing, and drying to obtain Ca-Mg-Zn-Al hydrotalcite; and (C) calcining to 600-800 degrees C for 3-8 hours.
NOVELTY - The method involves pressurizing a supplying biomass (200) from tank (110), in pumps (120). Biomass is preliminarily heated in heat exchanger (130) at specific temperature. Preheated biomass is reheated in reactor (140) using microwave radiation emitted by generators (150) through radiators (143). Temperature of biomass inside reactor is measured using temperature sensors (141) and controller (152). Power of radiation generated by generators is adjusted to retain biomass inside the reactor at specific temperature, based on measurements of temperature sensors and reflectometers.    USE - Method for hydrothermal liquefaction of biomass, using energy sources such as gas or oil burners, electric heating system, etc.    ADVANTAGE - As the power of radiation generated by generators is adjusted to retain biomass inside the reactor at specific temperature, based on measurements of temperature sensors and reflectometers, the hydrothermal liquefaction of biomass can be efficiently performed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for hydrothermal liquefaction of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for hydrothermal liquefaction of biomass with compact system of exchanger and reactor chambers.    Tank (110)    Pump (120)    Heat exchanger (130)    Reactor (140)    Temperature sensor (141)    Radiator (143)    Generator (150)    Controller (152)    Biomass (200)
NOVELTY - Treating biomass as a fuel in a plant (1) comprising rotary kiln (4) and the calciner (5) for producing cement clinker from raw meal, comprises pre-drying the biomass by the exhaust gases of a heat exchanger (2) in the plant, and charring the biomass in a reactor (17). The exhaust gas from the rotary kiln and the calciner is used for charring in the circuit.    USE - The method is useful for treating biomass as a fuel in plant for producing cement clinker from raw meal.    ADVANTAGE - The method utilizes low-calorific-value to process the biomass, and produces fuel in energy efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for plant for producing cement, comprising a device for treating biomass, a reactor, and heat exchanger comprising rotary kiln and the calciner.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the plant for treating biomass.    Plant (1)    Heat exchanger (2)    Rotary kiln (4)    Calciner (5)    Reactor (17)
NOVELTY - Composting container (100) comprises: a body (102) defining a cavity (104) for receiving material to be composted; a grating situated in the cavity, where the grating divides the cavity into an upper portion and a lower portion; and an agitator mechanism for agitating the material in the cavity.    USE - The container is useful for the decomposition of organic matter into compost, which is useful as a fertilizer or soil additive, where the organic matter includes waste vegetation and foods.    ADVANTAGE - The container simply and effectively facilitates the composting of organic matter in an eco-friendly manner, is portable by virtue of its wheels, and can be moved to a desired location (e.g. a garden) to access the compost material.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of a composting container.    Composting container (100)    Body (102)    Cavity (104)    Handle (114)    Wheel (116)    Recesses. (132)
NOVELTY - Gasifying carbon containing feed-stocks, preferably biomass, comprises tempering plant parts used during gasifying, by a molten salt.    USE - The method is useful for gasifying carbon containing feed-stocks, preferably biomass (claimed).    ADVANTAGE - The method can be performed with improved temperature control. The tempering method allows a simple and robust design of the cooling- or heating devices, where inexpensive materials can also be used. The method provides a low mechanical wear. The method uses cooling system that can be designed for low pressure.
NOVELTY - The utility model claims a carbonization processing device, especially relates to a kind of a dead animal pests carbonating device, comprising a dead pest animal corpse for pyrolysis of pyrolysis charring device, wherein the device is provided with pyrolysis carbonization chamber and a combustion chamber, a carbonization chamber is provided with a pyrolysis tank and the carbonization tank to heat or cool a circulating space, the carbonization chamber and the combustion chamber through the space and is connected with the circulating connection port connected with the combustion chamber and the carbonization chamber, the pyrolyzing tank is closed bottom end is provided with a pyrolysis gas outlet pipe, gas guide pipe is connected with the carbonization pot, the other one end of the air guide pipe is located in the combustion chamber, the carbonization can be opened or closed tank is provided with a tank door, a combustion chamber is provided with an air vent. This utility model device is energy-saving and environment-friendly, carbide yield is high.
NOVELTY - The utility model claims a kind of biological diesel oil production device, specifically to a method for improving a conversion rate of the device, comprising a liquid inlet pipe (1), a reaction kettle (2), a heating device (3), a mixing liquid circulating device and a liquid spraying device, wherein the mixed liquor circulation device is composed of peristaltic pump (8), a liquid conveying pipe (9), a mixing liquid circulating conveying pipe (9) is provided with the lower end of the peristaltic pump (8), the peristaltic pump (8) and the reaction kettle (2) at the lower end of a liquid outlet pipe (6) connected with the mixing liquid conveying pipe (9) of the upper end of the reaction kettle (2) and is connected with the middle upper part of reaction kettle (2). The utility model can obviously improve the biological diesel conversion rate, the reaction time is greatly shortened, the production efficiency is high, good quality and high yield and high economic benefit.
NOVELTY - The dual absorber electrode (100) comprises a first absorber material (102) having a first band gap, and a second absorber material (104) deposited on the surface of the first absorber material, and having a second band gap larger than the first band gap. The first absorber material is a silicon nanostructure, and the second absorber material is a hematite thin film deposited on the surface of the silicon nanostructure.    USE - Dual absorber electrode for water splitting to generate hydrogen and oxygen.    ADVANTAGE - Reduces or eliminates dependence on external applied bias, and achieves necessary voltage for water splitting, by efficiently utilizing solar spectrum and generating greater photovoltage. The utility of hematite improves using direct coupling with small-band gap materials to more efficiently utilize solar spectrum and to enhance photovoltages attainable by a single device.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device for splitting water to generate hydrogen and oxygen; and    (2) a method of fabricating dual absorber electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional view of the dual absorber electrode.    Dual absorber electrode (100)    First absorber material (102)    Second absorber material (104)    Electrical contact (106)
NOVELTY - The system has a male endplate (30a) comprising a first longitudinal side with a male alignment detent (52) of the male endplate and a male endplate electrode, where the male alignment detent of the male endplate fits within a female alignment detent (50) of an adjacent membrane frame of multiple membrane frames (54). Another membrane frame of the membrane frames are provided adjacent to the male endplate such that the female alignment detent of the latter membrane frame is received within the female alignment detent of the adjacent male endplate.    USE - Modular electrolysis system for converting electrolyte fluid into disassociated gases such as hydrogen and oxygen gases.    ADVANTAGE - The electrode frames, the membrane frames, the male endplate and the female endplates are immersed in a cooling water bath during operation of the system so as to maintain uniform temperature of the system and to extract heat from the system, thus increasing productivity of the system. The gas production chamber is fluidly connected at an uppermost portion to one of a first gas collection conduit or second gas collection conduit so as to remove produced gases from the system. The system utilizes nickel (Ni) coated electrodes so that operating voltage of the system at same temperatures is reduced about 2.7V/1.8V, thus reducing physical size of the system without reduction in system performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a cutaway view of a modular electrolysis system.    Male endplate (30a)    Female alignment detent (50)    Male alignment detent (52)    Membrane frames (54)    Passive electrode frames (56)
NOVELTY - The method involves providing an absorption signal comprising collected sunlight that has undergone absorption by a trace gas such as carbon dioxide (CO2), methane (CH4) and carbon monoxide (CO). The absorption signal is mixed with laser light at a nearby frequency to the absorption signal, where amplitude of a resulting RF signal is proportional to the concentration of the trace gas. The concentration of the gas is resolved at different altitudes by collecting an entire absorption feature. Changes in the amplitude of the RF signal are analyzed to determine changes in the gas concentration.    USE - Method for detecting concentrations of trace gas such as CO2, CH4 and CO (all claimed), in the atmosphere.    ADVANTAGE - The method ensures utilizing a laser heterodyne radiometer to measure CO2, CH4, and O2 in the atmospheric column, which is relatively small in size and inexpensive, and a luggage sized package that can be coupled to an AERONET aerosol sensor easily. The concentration of trace gases in the atmosphere is determined by measuring the absorption of sunlight in the infrared in an accurate manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a laser heterodyne radiometer    (2) a system for detecting trace gas concentrations in the atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for detecting trace gas concentrations in the atmosphere.    Sunlight (10)    Optical system (14)    Weak input signal (18)    Laser heterodyne radiometer (20)    System for detecting trace gas concentrations in atmosphere (100)
NOVELTY - This utility model is a kind of biomass gasification copper smelting system, belonging to the biomass comprehensive utilization field, comprising a raw material storage bin, a raw material spiral conveyor, a bed material bin, a bed material spiral conveyor, ash discharging device of gasification furnace, an air distribution plate, an air inlet, a cyclone dust remover, a spray tower, a gas-liquid separator, a draught fan, an auxiliary fuel pipe, a main fuel pipe, air pipe, a smelting furnace. It is added into biomass gasification furnace hearth according to raw material spiral conveyor, the pyrolysis and gasification reaction in the gasification furnace to generate gas by cooling and purifying into a smelting furnace and auxiliary fuel mixed combustion to provide heat source for melting the copper. This utility model combined with biomass fuel gas and biomass gasification, a biomass fluidized bed gasification, biomass fuel gas purifying and biomass gas burning and so on technology, the biomass fuel energy for use.
NOVELTY - Method for manufacturing bio-oil involves pulverizing biomass to prepare biomass-derived raw material, mixing the biomass-derived raw material, catalyst component, and acid, and reacting mixture for 0.1-10 hours on condition of 0.1-10 MPa of hydrogen pressure, and 373-573 K.    USE - The method is useful for manufacturing bio-oil (claimed).    ADVANTAGE - The prepared bio-oil can be reuse and cost-effective.
NOVELTY - The method involves supplying electricity to an electrolyte electrode assembly in a state where a fuel electrode is hydrogen-reduced. The fuel electrode is made to impregnate solution containing a sintering inhibiting agent, which prevents sintering of a particle of nickel and nickel oxide. The electrolyte electrode assembly is heat-processed in hydrogen gas atmosphere at temperature higher than temperature of the fuel electrode when a solid oxide fuel cell (SOFC) after completion is operated in hydrogen gas atmosphere.    USE - Method for manufacturing an SOFC i.e. fuel electrode support type SOFC.    ADVANTAGE - The method enables the fuel electrode to impregnate the solution containing the sintering inhibiting agent, so that sintering of the nickel particle is prevented by supporting the sintering inhibiting agent on a surface of the nickel particle even if the SOFC is operated at high temperature, thus achieving improvement of electric power generation and formation of long-term durability of SOFC, and preventing deterioration of structural units other than the fuel electrode of the SOFC.    DETAILED DESCRIPTION - The sintering inhibiting agent is nanoparticle of a ceria. An INDEPENDENT CLAIM is also included for an SOFC.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph representing a result of an endurance test of SOFC before and after impregnating a sintering inhibiting agent.'(Drawing includes non-English language text)'
NOVELTY - The hydrogen generating apparatus has a reaction container which accommodates a granular catalyst (P1,P2). A support portion is arranged inside the reaction container to support the catalyst. A projection portion is arranged at an edge of a support portion opening, and protruded to gravitational direction up side. The support portion opening formed in the support portion is larger than particles of the catalyst. A projection portion opening formed in the projection portion is larger than particles of the catalyst.    USE - Hydrogen generating apparatus used in fuel cell system.    ADVANTAGE - Since the fall of one catalyst can be suppressed, as the projection portion is protruded to the gravitational direction up side in support portion, the capability fall of the hydrogen generating apparatus can be prevented. The crushing-under-pressure of the catalyst can be suppressed, by making catalyst layer height of the catalyst portion small.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a catalyst filling method of a hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the modification vessel portion of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modification portion (20)    Modification portion inner cylinder (50)    Modification portion outer cylinder (51)    Catalyst upper space (60)    Granular catalysts (P1,P2)
NOVELTY - The apparatus (100) has a helical structured mixed gas path which supplies the mixed gas of source gas and water. A modification-catalyst layer generates the reformed gas containing hydrogen by carrying out steam reforming reaction of the supplied mixed gas. A helical structured reformed-gas path supplies the generated reformed gas. The water contained in the mixed gas is evaporated by heat-exchanging between the mixed gas path and the reformed-gas path.    USE - Hydrogen generating apparatus used for electric power generation of fuel cell.    ADVANTAGE - The size of the hydrogen generating apparatus can be reduced. The heat exchanging efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modification vessel structure. (Drawing includes non-English language text)    Water feed route (2)    Material supply path (3)    Air feed route (5)    Modification portion (6)    Hydrogen generating apparatus (100)
NOVELTY - Producing fuel briquettes comprises crushing wood wastes followed by mixing and pressing the wood wastes having a humidity of 40-50%, grinding the wood wastes to a size of less than 1-4 mm and heat treating at 240-250 degrees C to form briquettes with a density of 1200-1300 kg/m3.    USE - The method is useful for producing fuel briquettes (claimed).
NOVELTY - A method for producing biogas involves anaerobically digesting organic matter in methane fermentation tank, followed by electrical activation of medium and agitating, where electrical activation is accomplished by applying continuously constant voltage of 0.2 to 36 V through methane fermentation tank from electrically conducting material, which serves as cathode and anode placed inside the medium of methane fermentation tank and isolating from it by ion permeable material.    USE - For producing biogas (claimed).
NOVELTY - The method involves positioning a surface material (10) with sensors (22) for measuring the temperature of the material at different measuring points, and generating a heat flux from a heat source (21). A mapping of target and actual surface temperatures of the material is determined by a computer unit. Actual thermal conductivity of a thin anisotropic material is determined by adjusting theoretical thermal conductivity and minimizing difference between the target temperature and the actual temperature for each measuring point of temperature.    USE - Method for measuring thermal conductivity of a thin anisotropic material that is used for manufacturing a fuel cell and an electrolyzer.    ADVANTAGE - The actual thermal conductivity of the thin anisotropic material is determined by adjusting theoretical thermal conductivity and minimizing the difference between the target temperature and the actual temperature for each measuring point of temperature, thus measuring the thermal conductivity according to three directions such as transverse thermal conductivity, longitudinal thermal conductivity and thermal conductivity in the thickness in only one experimental operation on the same sample without assembling or disassembling of the sample, and ensuring reproducibility of the conditions of measurement and possibility of carrying out multiple constraints of tightening without dismounting the sample, and allowing to increase precision of thermal conductivities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a positioning tool for measuring thermal conductivity of a thin anisotropic material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a positioning tool for measuring thermal conductivity of a thin anisotropic material.    Surface material (10)    Heat source (21)    Sensors (22)    Positioning tool (200)    Upper plate (220)
NOVELTY - A microwave biochar gasification method involves carrying out pyrolysis of biomass feed material to convert the material to biochar. The biochar is mixed with catalyst and crushed to obtain mixture. The mixture is transferred to gasification reactor, followed by using microwave as heat source to heat the mixture in a protection of inert gas atmosphere to a desired gasification temperature, completely removing volatile component in the biological carbon, changing inert gas to gasification agent, and carrying out gasification reaction to generate synthesis gas after cooling.    USE - Method for gasification of microwave biochar for preparing synthesis gas.    ADVANTAGE - The method enables gasification of microwave biochar with improved production efficiency and quality of the synthesis gas, reduced emission of carbon dioxide and reduced energy consumption in a simple and inexpensive manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a method for gasification of microwave biochar.'(Drawing includes non-English language text)'
NOVELTY - A bio-oil prepared catalyst catalyzing and liquefying method involves mixing straw, low carbon alcohol solvent and magnetic catalyst into a high pressure kettle, heating to obtain the straw liquefied product and biological oil and its residue. The slag is dried. The filtrate is distilled and filtered to obtain liquid product. The resulting residue is graded into autoclave, heated to predetermined temperature and maintained for certain time to obtain liquefied bio-oil and residue, and the steps are repeated followed by performing straw grading catalyzing and liquefying bio oil.    USE - Method for catalyzing and liquefying bio-oil prepared catalyst.    ADVANTAGE - The method enables improving the utilization rate of catalyst and a rate of the biomass.    DETAILED DESCRIPTION - A bio-oil prepared catalyst catalyzing and liquefying method involves mixing straw, low carbon alcohol solvent and magnetic catalyst into a high pressure kettle, rapidly heating to the certain temperature and keeping for a certain time, to obtain the straw liquefied product and biological oil and its residue. The slag is dried at 100-105 degrees C under vacuum. The filtrate is distilled and filtered to obtain liquid product as biological oil. The resulting residue is graded i.e. catalytic residues, lower alcohol solvents, and magnetic catalyst (CaO-Al2O3-Fe3O4) into the autoclave, heated to a predetermined temperature and maintained for certain time after the reaction to obtain liquefied bio-oil and residue, and the steps are repeated followed by performing straw grading catalyzing and liquefying bio oil, where low carbon alcohol solvent is 1-5C alcohol, the ratio of the straw mass and catalyst mass is 10:1-30:1, and the molar ratio between the low carbon alcohol solvent volume (ml) and the catalyst mass (g) is 10: 1-30: 1.
NOVELTY - The magnetic valve has a casing (C) provided with a closing valve seat section (10). A valve portion (V) is provided with magnetic material. A driving permanent magnet (m) is adapted to be movable in the axial direction of the casing, and provided with magnetic poles at both ends in axial direction. A first yoke (4) consisting of ferromagnetic material is provided on side of closing valve seat section. Magnetic flux path is formed by the driving permanent magnet, the first yoke and the valve portion.    USE - Magnetic valve used for hydrogen fueled engine, piping system of hydrogen supply system for supplying hydrogen to fuel cell, semiconductor manufacturing apparatus and aerospace application.    ADVANTAGE - The strength of attachment of the valve portion with respect to the closing valve seat section is increased. The position retention strength of the permanent magnet for drive can act onto the valve strongly, so that fluid leakage can be prevented reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the valve-seat portion.    First yoke (4)    Closing valve seat section (10)    Casing (C)    Valve portion (V)    Driving permanent magnet (m)
NOVELTY - Increasing the rate of methanogenesis in a petroleum reservoir comprising methanogenic microbial consortia and foundation water, comprises: injecting a solution of stimulants comprising ammonium and phosphate ions into reservoir through a well head, in amount such that their concentration in at least a portion of reservoir is above critical concentration to effect enhanced methanogenesis but at a non-lethal level to methanogenic microbial consortia; and maintaining reservoir. The concentrations of ammonium and phosphate ions injected through well head are up to saturation concentration.    USE - The method is useful for increasing the rate of methanogenesis in a petroleum reservoir.    ADVANTAGE - The method: increases the rate of methanogenesis in a petroleum reservoir comprising methanogenic microbial consortia and foundation water, by utilizing ammonium and phosphate ions at a non-lethal level to methanogenic microbial consortia (claimed); exponentially increases methane production and provides at least 25 MCF, preferably at least 50 MCF per day under optimal conditions; utilizes methanogens which are hard and tolerate concentrations of nutrients; and increases the distance penetrated by the nutrient to provoke the desired rate of accelerated methanogenesis.
NOVELTY - This utility model is a household garbage for producing gas and/or fuel gas power generation, and the pyrolysis reaction kettle device, burning furnace, a lifter, a condenser, a gas-liquid separator, a tank, a gas purifying device, a gas blower, a gas cabinet and gas generating set composed of a horizontal, belongs to a kind of household garbage and high temperature particulate heat carrier in close oxygen-free of the horizontal rotary in the pyrolysis reaction kettle directly contact dry distillation pyrogenation production does not contain a fuel gas with higher calorific value, continuous production, no coking, high efficiency in the production without generating dioxin;
NOVELTY - This utility model is a kind of waste gas and gas generating device, the device generating a set a sewage purifying device is composed of a pressure safety alarm device, temperature automatic control device, a gas monitoring device, a, a drier, a pyrolyzing gasification furnace, a gas purifying device, a gas cabinet, the gas, the utility model has the following advantages: (1) it can control the pressure of the production process, the temperature, the gas standard gas automatic alarm, (2) to the garbage containing water is converted into gas and gas output, and continuous production, (3) belonging to the anoxic destructive distillation technology, the gas product containing a , (4). The utility model device belongs to commodity normal to the industry, the operation is reliable, the technology is mature, simple structure, convenient maintenance, low cost, (5) the garbage to transform into human urgently needed energy source (gas or electric power) and large-scale injection molding is carried out the domestic garbage reduction, harmless and energy in use, has good industrial practicability.
NOVELTY - This utility model is a kind of waste gas and gas generating device, the device generating a machine and drier for dewatering machine, a drier, a pyrolyzing gasification furnace, a gas purifying device, a gas cabinet, the gas tail gas purifying device, this utility model with the prior art device has the following advantages: (1) the water with low heat value waste are converted into fuel gas and fuel gas power generation, (2) oxygen-free or anoxic destructive distillation technology, the gas product containing a , (3). The utility model device belongs to commodity normal to the industry, the operation is reliable, the technology is mature, (4) the utility model can put garbage into fuel gas or fuel gas to generate power and large-scale injection molding is carried out the domestic garbage reduction, harmless and energy in use, has good industrial practicability.
NOVELTY - The sewage treatment unit has a membrane processing apparatus that stores living organism proliferation medium which decomposes pollutant material and sludge. The excessive sludge is separated by the solid-liquid separator. The membrane processing apparatus is installed in the downstream of the solid-liquid separator and the sludge reformation machine.    USE - Sewage treatment unit used for purification of waste water such as sewage and industrial wastewater.    ADVANTAGE - The quality of the treated sewage is improved, the quantity of the process sludge is reduced, the generation of odor in the process sludge is prevented and the deterioration and fouling of a separation membrane are prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage disposal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow sheet illustrating the installation of sludge reformation machine and solid-liquid separator. (Drawing includes non-English language text)    Motor operated valves (1,2)    Waste-water transfer-pump (P1)    Submersible-pump (P2)    Pump (P3)
NOVELTY - Selective preparation of a fatty acid alkyl ester involves providing a liquid medium comprising one or more 4-26C fatty acids, one or more 1-3C alcohols and native patatin and allowing the fatty acids to react with the alcohols to obtain the fatty acid alkyl ester.    USE - The methods are useful for selectively preparing a fatty acid alkyl ester; and for producing biodiesel (all claimed).    ADVANTAGE - The method can accommodate large amounts of free fatty acids, function with a water content in the reaction medium of up to 91 vol.%, and produces products with high purity and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing biodiesel, comprising mixing patatin with a fatty acid feed stock and with one or more 1-3C alcohols, where the fatty acid feed stock comprises one or more 4-26C fatty acids, and allowing the one or more fatty acids to react with the one or more alcohols.
NOVELTY - Device comprises at least one electrode and ammonia producing cells disposed on the electrode.    USE - The device is useful for producing ammonia (claimed).    ADVANTAGE - The device produces ammonia at ambient temperature and pressure with less energy intensive and less environmentally taxing. The production of ammonia reduces transportation costs. The ammonia is produced naturally using biological organism. The method is environmentally-friendly, and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing ammonia, involves providing at least one device comprising at least one electrode and ammonia producing cells disposed on the electrode, providing the cells with an appropriate nitrogen-containing enzyme substrate, and producing ammonia from the cells; and    (2) system comprising device comprises at least one working electrode, at least one counter electrode, and at least one electrolyte solution, and optionally at least one reference electrode.
NOVELTY - Seed, soil, or plant treatment composition comprises a mineral lactate compound or a cobalt compound, and a pesticide, an inorganic fertilizer and/or a biological fertilizer.    USE - The composition is useful for treating seeds, soil or a plant to promote seed growth, germination, Azotobacter growth in the soil and plant growth against drought resistance (all claimed). Tests details described but no results given.    ADVANTAGE - The composition has high bioavailability, improves the quality of the soil, plant health, plant emergence, crop yield and plant resistance to disease and drought, minimizes physical damage to plants, reduces application and handling costs and time for farmers, and cuts down on pesticide drift problems.    DETAILED DESCRIPTION - An INDEPENDENT claim is included for a method of treating seeds, soil or a plant, comprising applying the treatment composition to one or more of a seed, soil and a plant, where the treatment composition provides a mineral lactate product to promote one or more of seed growth, germination, Azotobacter growth in the soil, plant growth and drought resistance.
NOVELTY - New catalyst comprising iron, silver and cerium, is claimed. A mass ratio of silver and iron is 0.05-0.95 and a mass ratio of cerium and iron is 0.1-1.    USE - The catalyst is useful in the production of synthesis gas, which is useful for synthesizing a hydrocarbon such as methanol, dimethyl ether or paraffin.    ADVANTAGE - The catalyst enables efficient production of the synthesis gas in an economical manner while minimizing or avoiding the formation of side reactions of methane or carbon deposition and catalyst deactivation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the catalyst.
NOVELTY - A metal complex comprises polyhydric carboxylic acid compound, metal ion chosen from ions of metal chosen from group 2-13 of a periodic table, organic ligand which is coordinated to the metal ion in multiple positions, and 1C or 2C monocarboxylic acid compound. The content ratio of polyhydric carboxylic acid compound and monocarboxylic acid compound is 10:1-5000:1.    USE - Metal complex is used for adsorbent and occlusion material for adsorbing and occluding carbon dioxide, hydrogen, carbon monoxide, oxygen, nitrogen, 1-4C hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor and organic vapor in gas separation apparatus for gas motor vehicle, and separation material for separating methane, carbon dioxide, hydrogen, nitrogen, ethylene, methane, ethane, ethane, ethylene, propane, propene, oxygen, argon and air (all claimed).    ADVANTAGE - The metal complex has excellent adsorption, occlusion and separation abilities of gas, water resistance, and durability, and is capable of retaining high adsorption ability at high temperature and humidity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) occlusion material, which contains metal complex;    (2) gas storage apparatus, which consists of gas occlusion space in the inside of a pressure-resistant container in which airtight holding is possible, and equipped with entrance and exit of gas occlusion material internally to gas occlusion space;    (3) gas motor vehicle, which comprises an internal combustion engine in which a driving force is obtained with a fuel gas supplied from the gas storage apparatus;    (4) separation material, which comprises metal complex; and    (5) separation method, which involves contacting metal complex and mixed gas under pressure of 0.01-10 Mpa.
NOVELTY - Treating biomass containing nitrogen, preferably biomass containing chicken excrement, comprises (a) subjecting the biomass at a dry matter content of less than 70%, preferably less than 50%, to an ammonia fermentation, and (b) removing ammonia during the ammonia fermentation by a stripping gas and/or by precipitation, preferably as magnesium ammonium phosphate, from the biomass.    USE - The method is useful for treating biomass containing nitrogen, preferably biomass containing chicken excrement (claimed).    ADVANTAGE - The method is capable of treating the biomass containing chicken excrement with less effort.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for treating biomass containing nitrogen, preferably for executing the method, comprising at least one container, which is suspended and/or fixed on a support and/or contains immobilized microorganisms and/or enzymes for ammonia fermentation.
NOVELTY - The apparatus has first heater (4) operated while second heater (4) is stopped, at first condition. Second heater is operated while first heater is stopped, at second condition. If detection values of first and second temperature detectors (5,6) are outside and beside first and second temperature ranges, respectively, heaters are operated at second condition. At both conditions, if detection values of respective detectors are outside first and second temperature ranges, starting determination of abnormality is performed, while carrying out abnormality alerting and shutdown of system.    USE - Catalytic reaction apparatus such as hydrogen generating apparatus for fuel cell. Can also be used in plant which manufactures chemical composition.    ADVANTAGE - The component abnormality can be specified easily and reliably, and it becomes possible to operate or stop the apparatus safely in the operating temperature limits of catalyst or reactor, even if a heater and a temperature detector have abnormality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of catalytic reaction apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the catalytic reaction apparatus.    Catalyst regions (1,2)    Heaters (3,4)    Temperature detectors (5,6)    Controller (7)
NOVELTY - Producing a monoalkene, comprises converting an alkyl monoester (I) into a monoalkene (II), by an enzymatic elimination of a molecule.    USE - The method is useful for producing a monoalkene i.e. ethylene, methyl ethylene, but-1-ene, but-2-ene or 2-methylprop-1-ene (all claimed), which is useful as fuel or as precursor of synthetic resins.    ADVANTAGE - The method: is environmentally friendly; and utilizes the enzyme, which exhibits improved enzymatic activity and stability even at increased temperature conditions.    DETAILED DESCRIPTION - Producing a monoalkene, comprises converting an alkyl monoester of formula ((R1)(R2)(X1)C-CH(R3)(R4)) (I) into a monoalkene of formula ((R1)(R2)C=C(R3)(R4)) (II), by an enzymatic elimination of a molecule X1H.    R1-R4 = -H, -CH3 or -C2H5; and    X1 = O-PO3H2, O-PO2H-O-PO3H2 or O-SO3H.    INDEPENDENT CLAIMS are also included for:    (1) a recombinant organism, which is capable of producing an alkyl monoester, and expresses an enzyme; and    (2) a composition comprising the organism, or the alkyl monoester and the enzyme.
NOVELTY - Energy supply unit comprises a wind turbine (1) for generating electric current from wind; an electrolysis device (4) for producing hydrogen and oxygen from water using at least a portion of the electric current generated by the wind turbine; a bioreactor (3) for producing methane from hydrogen and carbon dioxide using methanogenic bacteria, which is installed in a tower (2) of the wind turbine, and has a height of greater than 5 m; a feeding device for feeding carbon dioxide into the bioreactor; and an outlet provided in the bioreactor for biomethane-containing gas produced in the bioreactor.    USE - Used as an energy supply unit.    ADVANTAGE - The energy supply unit provides energy obtained from renewable energy sources without severe power fluctuations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for operating the energy supply unit, comprising (a) operating the wind turbine for generating electric current from the wind, (b) operating the electrolysis device for producing hydrogen and oxygen from water using at least the portion of the electric current generated by the wind turbine, (c) operating the bioreactor installed in the tower of the wind turbine, for preparing methane from hydrogen and carbon dioxide using methanogenic bacteria, (d) supplying hydrogen into the bioreactor and/or forming hydrogen in the bioreactor, (e) supplying carbon dioxide into the bioreactor, and (f) discharging the biomethane-containing gas obtained in the bioreactor, by an outlet provided in the bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the energy supply unit.    Wind turbine (1)    Tower (2)    Bioreactor (3)    Electrolysis device (4)    Network controller (11)
NOVELTY - An apparatus for treatment of palm oil mill effluent comprises 1st chamber (12) with inlet manifold placed at floor of chamber and outlet port (3) to remove waste sludge, and 2nd chamber which is separated from 1st chamber by divider gauge (16) and includes biofilm media which is capable of being suspended in waste liquid, restrainer unit (24) which is positioned at upper portion of chamber to prevent floating away of biofilm media, outlet port which discharges treated effluent and is positioned above the restrainer unit to carry away biogas (24) and discharge port (26).    USE - An apparatus for treatment of palm oil mill effluent (claimed).    ADVANTAGE - Hydraulic retention times, tank size, land area, and capital costs are reduced.    DETAILED DESCRIPTION - An apparatus for treatment of palm oil mill effluent comprises 1st chamber (12) with inlet manifold placed at floor of chamber and outlet port (3) to remove waste sludge, and 2nd chamber which is separated from 1st chamber by divider gauge (16) and includes biofilm media which is capable of being suspended in waste liquid, restrainer unit (24) which is positioned at upper portion of chamber to prevent floating away of biofilm media, outlet port which discharges treated effluent and is positioned above the restrainer unit to carry away biogas (24) and discharge port (26) to carry out outflow from 2nd chamber to 1st chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the anaerobic bioreactor tank.    Outlet port (3)    1st chamber (12)    Divider gauge (16)    Biogas (24)    Restrainer unit (24)    Discharge port (26)
NOVELTY - Preparation of insect biological fertilizer comprises: (A) mixing 40-60 pts. wt. manure, 20-30 pts. wt. mushroom waste, 20-30 pts. wt. crop straw, 0.5-1 pts. wt. mixed microbial agents, 3-5 pts. wt. nitrogen, 4-6 pts. wt. phosphate and 3-5 pts. wt. potash, and 0.2-0.4 pts. wt. micronutrient fertilizer, with water content of livestock manure of 40-60%, pH 6.5-7.5, crushing crop straw and mushrooms into 50-100 mesh sieve, and fermenting at 50-70 degrees C for 3-5 days.    USE - Method of preparation of insect biological fertilizer (claimed).    ADVANTAGE - The method is simple, and low cost.    DETAILED DESCRIPTION - Preparation of insect biological fertilizer comprises: (A) mixing 40-60 pts. wt. manure, 20-30 pts. wt. mushroom waste, 20-30 pts. wt. crop straw, 0.5-1 pts. wt. mixed microbial agents, 3-5 pts. wt. nitrogen, 4-6 pts. wt. phosphate and 3-5 pts. wt. potash, and 0.2-0.4 pts. wt. micronutrient fertilizer, with water content of livestock manure of 40-60%, pH 6.5-7.5, crop straw comprising millet straw, corn straw, soybean straw, sorghum straw and/or rice straw, ratio of carbon and nitrogen at 40-50:1, mixed microbial agents comprising beer yeast bacteria, Bacillus subtilis bacteria, Lactobacillus delbrueckii bacteria, Streptomyces bacteria, oxalic acid and Penicillium composition, and beer yeast bacteria containing Bacillus subtilis bacteria, Lactobacillus delbrueckii bacteria, Streptomyces bacteria, crushing crop straw and mushrooms into 50-100 mesh sieve, and fermenting at 50-70 degrees C for 3-5 days.
NOVELTY - 7-chloro-4-piperazinoquinoline is synthesized by carrying out condensation reaction of 4,7-dichloroquinoline and anhydrous piperazine at 90-150 degrees C for 1-4 hours, extracting with water-miscible organic solvent, drying, and concentrating.    USE - Method for synthesizing 7-chloro-4-piperazinoquinoline (claimed) for preparing medicines.    ADVANTAGE - The process is simple and easy.
NOVELTY - 1-Methylhydantoin is prepared by reacting sarcosine and sodium cyanate in water, and carrying out cyclization reaction with sulfuric acid.    USE - Method for preparing 1-methylhydantoin (claimed).    ADVANTAGE - The method has low cost.
NOVELTY - Cracking of kitchen microwave pyrolysis residue taken tar involves dehydrating kitchen garbage; drying at 90 degrees C for 5 hours until moisture content is not greater than 5%; subjecting kitchen waste residue to microwave cracking at 500 degrees C; uniformly mixing 5-15% kitchen garbage in microwave cracking reactor; introducing nitrogen for 20 minutes; reacting under anaerobic condition; condensing volatile component product; respectively collecting condensed product and non-condensed gas product; heating kitchen garbage at 500 degrees C to liquefy; and cracking for 5 minutes.    USE - Cracking of kitchen microwave pyrolysis residue taken tar.    ADVANTAGE - The method accelerates kitchen garbage microwave cracking process, effectively saves electric energy, and increases tar yield. It is simple and easy to perform, and produces microwave cracked residue that is recyclable and low cost.    DETAILED DESCRIPTION - Cracking of kitchen microwave pyrolysis residue taken tar comprises dehydrating kitchen garbage; drying at 90 degrees C for 5 hours until moisture content is not greater than 5%; subjecting kitchen waste residue to microwave cracking at 500 degrees C; uniformly mixing 5-15% kitchen garbage in microwave cracking reactor; putting into microwave cracking furnace; introducing nitrogen gas for 20 minutes; reacting under anaerobic condition; feeding volatile component product through first-stage condensing apparatus; collecting condensed product in collecting bottle; collecting non-condensing gas product in collecting bag; heating kitchen garbage at 500 degrees C to liquefy; cracking for 5 minutes; dividing collected liquid in bottle into two layers consisting of upper tar layer and lower weak alkali layer; and separating upper tar layer in storage bottle.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a process for cracking kitchen microwave pyrolysis residue taken tar (Drawing includes non-English language text).
NOVELTY - A bio-ethanol fuel oil contains 20-80 wt.% waste oil, 10-60 wt.% methylal, 20-80 wt.% methyl alcohol, 3-15 wt.% oleic acid, 0.05-5 wt.% Span 80 (RTM: Non-ionic surfactant, sorbitan oleate) and 0.5-5 wt.% potassium permanganate.    USE - Bio-ethanol fuel oil for restaurant stove.    ADVANTAGE - The bio-ethanol fuel oil is environment-friendly, low cost, stable, suitable alternative energy source, and has high calorific value and efficiency, low dust emissions, and no pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-ethanol fuel which involves heating waste oil at 50-70 degrees C, pouring melt into normal temperature and pressure tank, adding methylal followed by methyl alcohol, stirring for 5-15 minutes, adding oleic acid and Span 80 (RTM: Non-ionic surfactant, sorbitan oleate), stirring for 5-15 minutes, adding potassium permanganate, stirring for 5-15 minutes, standing for 15-30 minutes, and filtering.
NOVELTY - A microorganism fertilizer comprises phosphate rock, potassium ore, stone powder, peat powder, calcium superphosphate, potassium oxide, Aeromonas powder, Candida powder, Rhodococcus powder, steamed stuffed bun bacteria powder, Escherichia coli powder, Bacillus subtilis powder, radish cake, chicken manure, rice bran, and rare earth fertilizer.    USE - Microorganism fertilizer.    ADVANTAGE - The fertilizer is convenient to operate, simple to prepare, and nutritionally balanced, has high levels of viable cells and variety of enzymes, strong resistance, and high yield, and improves soil bacteria function and crop quality.    DETAILED DESCRIPTION - A microorganism fertilizer comprises 4-9 pts. wt. phosphate rock, 8-12 pts. wt. potassium ore, 15-25 pts. wt. stone powder, 24-35 pts. wt. peat powder, 14-23 pts. wt. calcium superphosphate, 1-6 pts. wt. potassium oxide, 0.01-0.02 pts. wt. Aeromonas powder, 0.01-0.02 pts. wt. Candida powder, 0.01-0.02 pts. wt. Rhodococcus powder, 0.01-0.02 pts. wt. steamed stuffed bun bacteria powder, 0.01-0.02 pts. wt. Escherichia coli powder, 0.01-0.02 pts. wt. Bacillus subtilis powder, 14-25 pts. wt. radish cake, 25-35 pts. wt. chicken manure, 14-23 pts. wt. rice bran, and 1-2 pts. wt. rare earth fertilizer.
NOVELTY - A system comprises supporting device (4), hydrogen oxygen device (1), input/output device, electrolysis device, solar plate (2), and wind power generator (3).    USE - System used for generating hydrogen and oxygen.    ADVANTAGE - The system has simple structure, utilizes wind renewable energy, has low cost, saves energy, and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of system.    Hydrogen oxygen device (1)    Solar plate (2)    Wind power generator (3)    Supporting device (4)    Input/output device (5)
NOVELTY - The system has a normal pressure hopper whose lower part is connected with a crusher for crushing biomass raw material particles. A gasification furnace is connected with a hot pressing device that is provided with an outlet. A material return valve is connected with the gasification furnace. Gas enters a tar separator for separating the tar. The gasification furnace is provided with a coke oil injector. A gas turbine output is used for discharging high temperature flue gas heat recovered by a waste heat boiler. A steam and power generating unit is used for generating electricity.    USE - Biomass pressuring fluidized bed gasification gas turbine combined cycle power generation system.    ADVANTAGE - The system is environment-friendly and suitable for using biomass energy in large scale, and has high gasification efficiency, high separating efficiency and generating efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass pressuring fluidized bed gasification gas turbine combined cycle power generation system.
NOVELTY - The exchanger has a four-way valve (2) provided with four outlets (2-1). A gas inlet (1) is connected with a gas outlet (7) whose ends are connected with a first heat exchanger unit (3) and a second heat exchanger unit (4). The first heat exchanger unit and the second heat exchanger unit are serially connected together and adopted with a microwave permeable tube. The first heat exchanger and a condensation layer unit are attached with a coke oil unit. The microwave permeable tube is a PTFE tube, a glass tube and a ceramic tube.    USE - Heat exchanger for cooling and recovering waste heat of tar rich biomass gasified fuel gas.    ADVANTAGE - The heat exchanger has heat-exchanging efficiency, and solves cooling and recovering waste heat recovering problem of tar rich biomass gasification gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a heat exchanger processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a heat exchanger.    Gas inlet (1)    Four-way valve (2)    Outlets (2-1)    Heat exchanger units (3,4)    Gas outlet (7)
NOVELTY - A micro-emulsified biodiesel oil comprises 87-92% biodiesel, 5-10% water, and 3% additive. The additive comprises 3-10% phthalocyanine ethanolamine phospholipid, 5-15% cellobiose glycolipid, 2-18% phospholipid fatty acid, 7-15% rhamnolipid, 12-25% Span 80 (RTM: sorbitan monooleate), 4-12% diethylene glycol, 5-12% propylene glycol, 3-10% isopropyl alcohol, 2-15% cholesterol and 9-20% ethanolamine.    USE - Micro-emulsified biodiesel oil for automobiles.    ADVANTAGE - The micro-emulsified biodiesel oil has secondary atomization effect at high temperature, suppressing the generation of harmful substances, nitrogen oxide and carbon dioxide. The biodiesel oil has excellent low temperature fluidity, thermodynamic stability, and can be regenerated easily.
NOVELTY - An anticorrosive agent comprises 30-60 wt.% coal ash, 10-30 wt.% aluminum sulfate, 20-50 wt.% kaolin and 10-20 wt.% calcium sulfate.    USE - Anticorrosive agent for biomass boiler (claimed).    ADVANTAGE - The anticorrosive agent is economical, has large specific surface area, improves the mechanical strength of the boiler, increases the reaction area of the alkali metals and chloride in the heating surface and reduces metal corrosion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the anticorrosive agent, which involves calcining coal ash, mixing calcined coal ash, aluminum sulfate, kaolin and calcium sulfate, extruding and baking.
NOVELTY - This utility model claims a kind of dry natural gas produced hydrogen device of double-circulation system according to claims, wherein the hydrogenation catalyst comprises a drying system and a dry agent system, the referred regeneration method of hydrogenation catalyst drying system comprises a pressing machine, a heating furnace, a reactor, reactor, cooler operation, wherein the desulfurizing drying system comprises a second compressor, a heat exchanger, a reformer, a change in reactor and cooler. Compared with the existing technology, the utility model advantages are as follows: the utility model saves the cost and time, it is convenient to use. Because a purchase a put hydrogen from refinery normal far away, and the reducing catalyst, the hydrogen cannot be interrupted, the hiring needs of liquid chlorine sampling steel bottle, according to a plurality of row of transport vehicle, wherein the storage safety of factory also as a. In addition, liquid ammonia hydrogen generated by pyrolysis, the cost is only a purchase bottled hydrogen of SEQ ID NO: 1/5.
NOVELTY - This utility model claims a three-section biomass gasification for low tar with high heating value gas of device, comprising a fluidized bed gasification reactor, a cyclone reforming reactor, moving bed catalytic reactor and returning device, the upper part of the fluidized bed gasification reactor cyclone upper part of the reforming reactor, a fluidized bed gasification reactor through the material returning device and a bed catalytic reactor is connected with the lower part of the cyclone reform the top of the reactor and moving bed catalytic reactor top. fluidized bed gasification reactor lower part is further provided with a biomass grain feeding port and the first oxygen/steam inlet, cyclone reforming reactor upper part of the second oxygen/vapour; returning device is the third rich oxygen/steam inlet. This utility model can effectively solve the biomass gasification process in the gas heat value, high concentration, preparing more than one gas can be directly applied to the device of a high quality fuel gas. A process capable of self-heating type gasification with low cost, and has high energy utilization rate.
NOVELTY - This utility model claims a high temperature and high pressure biomass synthesis gas cooling and purifying device, comprising a shell and a vertical waste heat boiler smoke tube waste heat boiler, the venturi washing tower and the wet electric dust catcher, waste heat boiler of the biomass gasification furnace is connected with the outlet of the synthesis gas, a waste heat boiler outlet pipe waste heat boiler air inlet port is connected with the vertical flue, the air inlet of the washing tower in the vertical smoke tube outlet is connected with venturi to waste heat boiler is connected with the venturi washing tower is connected with the wet electric dust catcher is connected with the input end of the output end of the wet electric dust catcher is connected with the air inlet of the air storage tank. This utility model adopts sectional cooling and afterheat recycling, realizing the collected as heavy tar, waste heat step recycling, improves the heat efficiency, using the venturi washing tower washing gas dust-removing, wet electric dust removing device and dust-removing and high pressure process to realize the biomass synthesis gas of dust and purifying aim the focus so that the dust content and tar content is less than 10mg/Nm3.
NOVELTY - Treating agriculture wastes based on cellulosic materials comprises treating with acid-base followed by secondary treatment with oxidizing agent to produce free active functionalities for immobilization of biomolecules.    USE - The method is useful for treating agriculture wastes based on cellulosic materials. The secondary treated sawdust with PI is useful for immobilizing biomolecules such as proteins, peptides, drugs, saccharides, lipids, nucleic acids and nucleotides, where the biomolecules used are proteins and especially enzymes. The novel treated cellulose waste is useful for binding to biomolecules through ionic interaction and/or crosslinking via covalent bonding (all claimed).    ADVANTAGE - The treated sawdust can solve an environmental problem, as well as can produce an excellent solution for production of cheap carriers. The immobilized enzymes can be reused for tens of times, which will reduce the cost of the enzymes and their products.
NOVELTY - Manufacture of pellet fuel involves collecting forest residue, drying, crushing and performing cold extrusion and molding.    USE - Manufacture of pellet fuel (claimed).    ADVANTAGE - The method efficiently provides pellet fuel having excellent stability and high calorific value.
NOVELTY - The biomass recycling chute has a reaction tank (1) whose bottom portion is provided with a spiral conveying device (2). The reaction tank is provided with a sludge conveying port (11) and a straw conveying port (12). Other side of reaction tank is provided with a mixture outlet (13). The domestic sludge conveying port and straw conveying port are provided with an air guide channel (3). The side wall of air guide channel is provided with a port (31) which is connected with the reaction tank. The bottom of reaction tank is provided with an exhaust port (4).    USE - Biomass recycling chute.    ADVANTAGE - As the waste gas in the boiler is reacted with straw and domestic sludge of reaction tank, the dust in the waste gas can be effectively removed. The energy consumption and environmental pollution of biomass recycling chute can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass recycling chute. (Drawing includes non-English language text)    Reaction tank (1)    Spiral conveying device (2)    Air guide channel (3)    Exhaust port (4)    Sludge conveying port (11)    Straw conveying port (12)    Mixture outlet (13)    Port (31)
NOVELTY - The boiler has a feeder (1) whose middle part is connected with a main body (2) that is connected with a primary gas-solid separator (3). A bottom part of a material returning valve (11) is connected with a lower part of the main body. The primary gas-solid separator is connected with a secondary gas-solid separator (4) that is connected with an ash bin (12). An inlet of the secondary gas-solid separator is connected with a fuel gas high-temperature combustion chamber (6) through a coal economizer (8). An air pre-heater (9) is connected with a tail gas channel (13).    USE - Biomass and dangerous solid waste gasification fluidized bed combustion boiler.    ADVANTAGE - The boiler has high energy utilization rate and large combustion temperature, and avoids coking and combustion corrosion phenomenon and reduces soil wastage rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass and dangerous solid waste gasification fluidized bed combustion boiler.    Feeder (1)    Main body (2)    Primary gas-solid separator (3)    Secondary gas-solid separator (4)    Fuel gas high-temperature combustion chamber (6)    Coal economizer (8)    Air pre-heater (9)    Material returning valve (11)    Ash bin (12)    Tail gas channel (13)
NOVELTY - This utility model claims a four-section type garbage combustible through continuous pyrolysis and pyrolysis gasifying furnace, four-section type garbage combustible through continuous pyrolysis and pyrolysis gasifying furnace comprises a base provided with a base of a power cleaning system which is set on the section of the gasification furnace body on the power cleaning system, a carbonization furnace in a gasification furnace body part, which is set on the drying section in a carbonization furnace body which is set on the feeding section of the furnace body and a furnace body which is set on the air outlet cover is pressed on the feeding section furnace body, and feeding device is set on the cover pressing device. Solves the garbage incineration method has a problem of environmental pollution, has energy-saving environment-friendly and so on.
NOVELTY - This utility model is a kind of biomass fluidized bed gasification combustion device, belonging to the technical field of biomass combustion, comprising a combustion air inlet, a secondary air inlet, an air interlayer, a secondary air opening, a Venturi nozzle, fuel feeding pipe cap, a primary air port, the uniform pressure chamber, a gasification air inlet, discharging pipe, a fluidized bed gasification chamber. Air inlet connected with the air interlayer is connected with the tangential secondary air inlet and a secondary air opening, gasification air inlet through the uniform pressure chamber cap and is connected with the air inlet, a fuel feeding pipe and discharging pipe are respectively installed on the side wall and bottom of gasification combustion room, the bottom chamber is provided with fluidized bed gasifying chamber, and the outlet is provided with a Venturi nozzle. This utility model biomass fluidized bed gasification burner adopts special technology and structure, at the same time improves the utilization efficiency of the biomass, which ensures the stability of the combustion, which solves the coke oil and slag in the biomass gasification process.
NOVELTY - A kind of straw gasification furnace, comprising a gas generator, a gas purifying device, a fuel gas combustion device, an air inlet device, a feeding device, an air inducing device, and the air outlet of the sealed cover, the gas generator is set with gas purifying device is set with fuel gas combustion device, a fuel gas combustion device and a gas purifying device on the sealing cover for gas valve vertically connected with gas combustion device with the air inlet device is provided with a air inlet pipe connected with the oxygen valve and an air inlet valve is connected with a flue gas discharge pipe is installed between the air blower, fuel gas combustion device and a gas purifying device for oxygen valve and an air inlet valve, a flue gas discharge pipe is equipped with flue gas discharge valve is set with a feeding device, a gas generator, a feeding device is composed of a crank shaft and a stirring frame, the lower bottom surface of the gas generator is set with air inlet device, an air inlet device with air outlet hole pipe tee joint, a plug, provided with an air inducing device, a gas generator side on the fuel gas purifying device and the bottom surface with water, the gas generator and the inner sleeve and outer sleeve water.
NOVELTY - A methanol gasoline is composed of 60-70 wt.% 90# gasoline, 24-30 wt.% methanol, 4-7 wt.% toluene, 1-3 wt.% dicyclopentadienyl iron and 1-3 wt.% benzoic acid.    USE - Methanol gasoline (claimed).
NOVELTY - A naphtha methanol gasoline comprises 52-60 wt.% naphtha, 30-46 wt.% methanol, 0.0003-0.0005 wt.% benzoic acid, 0.0005-0.0006 wt.% ferrocene and 1-2 wt.% iso-diol.    USE - Naphtha methanol gasoline (claimed).
NOVELTY - Preparation of biological diesel oil involves pre-processing catalyst and pulverizing to size of 100 meshes, calcining at 850 degrees C for 2 hours and obtaining calcium oxide powder, adding red mud and calcium oxide powder in mass ratio of 1:1 into distilled water, stirring, drying, baking and activating at 600 degrees C and obtaining solid alkali catalyst, mixing vegetable oil with methanol in presence of catalyst, stirring, heating and ester-exchanging for 5 hours and obtaining biodiesel, centrifuging and separating solid catalyst.    USE - Preparation of biological diesel oil (claimed).    ADVANTAGE - The method efficiently and economically provides biological diesel oil, with yield of more than 93% and performance index.    DETAILED DESCRIPTION - Preparation of biological diesel oil involves pre-processing catalyst and pulverizing to size of 100 meshes, calcining at 850 degrees C for 2 hours and obtaining calcium oxide powder, adding red mud and calcium oxide powder in mass ratio of 1:1 into distilled water, stirring, drying, baking and activating at 600 degrees C and obtaining solid alkali catalyst, mixing vegetable oil with methanol in presence of catalyst, stirring, heating and ester-exchanging for 5 hours and obtaining biodiesel, centrifuging and separating solid catalyst, allowing to standstill the liquid phase mixture to divide into layers, such that the upper layer is rough bio-diesel and lower layer is byproduct glycerol, and compressing distilling and purifying upper layer.
NOVELTY - Alcohol comprises 70-90 wt.% methanol, 0.31-1.6 wt.% auxiliary agent, 1-5 wt.% ethanol, 1.8-9 wt.% carbon-based additive, 0.01-0.l wt.% ammonia, and remainder of water.    USE - Alcohol is used for fuel (claimed) used in industrial boiler.    ADVANTAGE - The alcohol is environmentally-friendly and economical. The fuel containing the alcohol suppresses the emission of carbon monoxide and other toxic gases from industrial boiler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol, which involves preparing solution (A) by adding carbon-based additive to ethanol, preparing solution (B) by adding auxiliary agent into water and cooling, mixing both solutions, and stirring.
NOVELTY - An alcohol-modified additive contains 99.9989-99.9992 wt.% toluene, 0.0005-0.0006 wt.% dicyclopentadienyl iron and 0.0003-0.0005 wt.% benzoic acid.    USE - Alcohol-modified additive is used for methanol gasoline.    ADVANTAGE - The methanol gasoline containing the alcohol-modified additive has high octane number, stability, antiknock characteristics and pressure resistance.
NOVELTY - 53-60 wt.% Eucalyptus bark, 7-15 wt.% pine branches, 10-15 wt.% cassava stem, 5-10 wt.% straw, 5-10 wt.% sugar cane leaves and 10-15 wt.% pine bark are mixed and provided to carbonization kiln and calcined, to obtain semi-finished biomass product. The semi-finished biomass product is pulverized to 20 meshes. 85-90 wt.% Carbon black and 10-15 wt.% biological adhesive are added and uniformly mixed. 20 wt.% Water is added, stirred and provided to extruder and processed to form strip. The strip is cooled and packaged, to obtain biomass fuel.    USE - Production of biomass fuel used for industrial boiler.    ADVANTAGE - The method enables economical production of biomass fuel, without environmental pollution. The heat productivity of biomass fuel is 4500-5000 calories. The biomass fuel does not generate sulfur dioxide.    DETAILED DESCRIPTION - 53-60 wt.% Eucalyptus bark and branches, 7-15 wt.% pine branches, 10-15 wt.% cassava stem, 5-10 wt.% straw, 5-10 wt.% sugar cane leaves and 10-15 wt.% pine bark are mixed and provided to carbonization kiln at height of 120-l30 cm from the bottom. A layer of splintered off Eucalyptus bark and branches is paved to height of 30-40 cm and provided to kiln and calcined, to obtain semi-finished biomass product. The semi-finished biomass product is pulverized to 20 meshes. 85-90 wt.% Carbon black and 10-15 wt.% biological adhesive are added and uniformly mixed. 20 wt.% Water is added, stirred and provided to extruder and processed to form strip. The strip is cooled and packaged, to obtain biomass fuel.
NOVELTY - 4-Amino-6-chloro-1,3-bis sulfonamide and formaldehyde are reacted at 90-100 degrees C for 0.5-1.5 hours, and the reaction liquid is cooled after decoloring. The pH of the obtained mixture is adjusted to 5.5-7, separated and purified to obtain hydrochlorothiazide.    USE - Preparation of hydrochlorothiazide (claimed).    ADVANTAGE - The method efficiently and safely provides hydrochlorothiazide by simple method under mild reaction condition in short period of time without affecting the environment.
NOVELTY - Calcium oxide is calcined, ground and sieved, to obtain 10-200 mesh calcium oxide carrier particles. Pre-treated carrier particles and iron nitrate nonahydrate are mixed, agitated, dried, calcined, cooled to room temperature and ground. The resultant product is mixed with cerium nitrate hexahydrate, stirred, placed in muffle furnace, calcined, cooled to room temperature, ground, mixed with 0.1-1 g/ml zirconium nitrate pentahydrate, stirred, placed in muffle furnace, calcined, cooled, ground, molded and sieved, to obtain iron-based catalyst.    USE - Manufacture of iron-based catalyst for biomass gasification and pyrolysis (claimed).    ADVANTAGE - The method efficiently provides iron-based catalyst.    DETAILED DESCRIPTION - 10-100 g calcium oxide is placed in muffle furnace, calcined at 500-1000 degrees C for 2-10 hours, ground and sieved, to obtain 10-200 mesh calcium oxide carrier particles. 10-100 g Pre-treated carrier particles and 0.1-1 g/ml iron nitrate nonahydrate are mixed, agitated at 30-100 degrees C for 2-24 hours, dried at 100-200 degrees C for 10-20 hours, placed in muffle furnace, calcined at 500-1000 degrees C for 2-10 hours, cooled to room temperature and ground. The resultant product is mixed with 0.05-1 g/ml cerium nitrate hexahydrate, stirred at 50-120 degrees C for 2-24 hours and 100-200 degrees C for 10-20 hours respectively, placed in muffle furnace, calcined at 500-1000 degrees C for 2-10 hours, cooled to room temperature, ground, mixed with 0.1-1 g/ml zirconium nitrate pentahydrate, stirred at 40-110 degrees C for 3-12 hours and 100-300 degrees C for 20 hours respectively, placed in muffle furnace, calcined at 500-900 degrees C for 4-10 hours, cooled, ground, molded and sieved, to obtain iron-based catalyst having particle size of 30-40 mesh.
NOVELTY - Repairing soil and generating biofuel comprises planting rich in cellulose, lignin fast growing plants on soil polluted with metal mine; harvesting plant; carrying out pyrolysis to obtain carbon and pyrolysis oil, performing catalytic hydrogenation to pyrolysis oil to obtain fuel oil, impregnating biochar with hydrochloric acid or nitric acid, vacuum filtering, separating carbonized material from acid solution, rinsing bio-treated carbon with clean water, recycling for absorbing persistent organic pollutant in mine soil, and leaching acid solution.    USE - Method for repairing soil and generating biofuel (claimed).    ADVANTAGE - The method is low cost and environment-friendly.
NOVELTY - The method involves collecting biomass particles after performing crushing and sieving process to obtain diameter of the biomass particles. Grain is formed as the biomass particles. The obtained biomass particles are filled into a quick fluidized bed pyrolysis reactor. Quick pyrolysis reaction is performed at certain temperature of about 500-600 degrees centigrade to obtain a pyrolysis gas and solid carbon reaction product. Quick pyrolysis gas and solid carbon reaction product condensing process is performed. Purified non-condensable gas is formed as fuel gas or fluidizing gas.    USE - Comprehensive heavy chemical biomass energy pyrolysis biological oil preparing method.    ADVANTAGE - The method enables utilizing a heavy oil component for performing biological oil separation operation, realizing comprehensive heavy chemical biomass energy pyrolysis biological oil preparing process and improving oil quality.
NOVELTY - A device comprises granulator (2) connected to fan (4) and conical reactor (5) provided with a feeding port, discharge hole, and an air outlet which is connected to first separator (11) and condenser (10); a second separator (12), heat exchanger (7), refrigerator, water pump and pipeline.    USE - Device used for producing bio-oil (claimed).    ADVANTAGE - The device reduces production cost of biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bio-oil comprising entering liquid discharge slag from blast furnace at 1400-1550 degrees C into granulator, fan blowing cool air into granulator, granulating liquid slag into 2-3 mm grain diameter, heating solid state into 800-1000 degrees C, and crushing into 1-2 mm; mixing into conical reactor, carrying out fast biomass cracking gasification and thermal cracking to generate gas, solid slag formation and slag particles; passing biomass thermal cracking gas through first separator, separating into condenser, carrying out rapid cooling to obtain bio-oil, absorbing waste heat in heat exchanger to generate high temperature steam to drive refrigerator to work condensing high temperature steam, and pumping condensed water into condenser for cooling bio-oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device.    Granulator (2)    Fan (4)    Conical reactor (5)    Heat exchanger (7)    Condenser (10)    First separator (11)    Second separator (12)
NOVELTY - The method involves drying and crushing seaweed polysaccharide powder. Polysaccharide powder liquid is selected as raw material. Water is uniformly added in the raw material to obtain mixture. A reaction kettle is heated to obtain a solid-liquid product. Alkane and aromatic hydrocarbon liquid fuel is collected. A red algae seaweed is selected from group consisting of coral, agar, asparagus and gold algae. A brown algae seaweed is selected from group consisting of kelp, copper and iron nail. A green algae is selected from group consisting of ulva pertusa, spirogyra and anserine.    USE - Method for preparing polysaccharide liquid hydrocarbon fuel by liquefying biomass.    ADVANTAGE - The method enables preparing polysaccharide liquid hydrocarbon fuel in simple and environment-friendly manner with mild reaction condition, low oxygen content and improved liquid fuel heat value.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating relationship between for polysaccharide liquid hydrocarbon fuel preparing characteristics. '(Drawing includes non-English language text)'
NOVELTY - Frictional drag thermal cracking treatment of domestic garbage comprises sealing domestic garbage in friction thermal cracking device, extruding by friction screw unit; sending garbage to rotor friction drag unit, friction dragging to generate frictional heat and drag force, carrying out pyrolysis to domestic garbage to obtain mixed product; settling mixed product, separating solid product comprising carbon ash; gas-liquid separating the rest of mixed product obtain gas, oil and water.    USE - Method for frictional drag thermal cracking of domestic garbage (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has zero discharge.
NOVELTY - The method involves forming a down-suction fixed bed gasification furnace with a raw material. A material gasification furnace top is connected with a gasification furnace top cover inner side. Softening expansion devolatilization process is performed. A lower part of down-suction fixed bed gasification furnace is connected with a black liquor semi-coke reducing layer. Reduction temperature is maintained at 850 degrees centigrade. Aqueous solution is obtained. The obtained aqueous solution is filled to a caustic chemical section. The caustic chemical section is connected with a gas outlet.    USE - Rice wheat straw soda pulping black liquor gasification solid alkali recycling method.    ADVANTAGE - The method enables reducing construction cost and ensuring simple operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rice wheat straw soda pulping black liquor gasification of solid alkali recycling device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view illustrating a rice wheat straw soda pulping black liquor gasification solid alkali recycling method.
NOVELTY - A biological-based methanol gasoline additive comprises component comprising 4-6% fatty alcohol and 2-5% alkane, low-temperature anti-freeze component comprising 6-8% yeast 16-18C fatty acid, oleic acid, or oil extracted from EAM-AC16 fermented yeast strain, and low-boiling component comprising 75-80% fatty alcohol, 6-8% butter fat, and 81-88% n-4C fatty alcohol. The fatty alcohol is heterogeneous medium-carbon 3-4C alcohol, preferably isopropyl alcohol, or isopropyl alcohol and isobutyl alcohol in volume ratio of 2:1 a mixture. The alkane is isooctane.    USE - Biological-based methanol gasoline additive (claimed).    ADVANTAGE - The biological-based methanol gasoline additive has high compatibility, low-temperature freeze-proof property, and stability.
NOVELTY - This utility model claims an evaporator with a liquefied methane rectifying tower, comprising tower body, tower kettle, sub-cooler, an evaporator, a corrugated plate filler, a liquefied methane inlet pipe, the evaporation mixing gas pipe, super-cooling liquid pipe, a non-condensable gas outlet pipe of purified liquefied methane discharging pipe, the utility model adopts a evaporator tower kettle middle part, an evaporator connected to the left side of a liquefied methane inlet, right side is connected with the evaporation of a mixed gas pipe, makes full use of the liquefied methane evaporation release, high efficiency rectification liquefied methane, and device is simple in structure, convenient to operate, and the liquefied methane purity is high, the utility model can effectively separating and purifying liquefied methane from liquefied methane.
NOVELTY - This utility model claims a kind of wood cellulose biomass raw material steam explosion device, comprising a washing machine, a washing machine connected with the blade pump is connected with the separator, the liquid phase outlet of the separator is connected with the washing machine, the solid phase outlet of the boiler is connected with separator, boiler is connected with pentose separator, pentose separator solid phase outlet is connected with a buffer tank, buffer tank is connected with the spraying tank, the spraying tank is connected with is connected with the collector. A complete set of device comprises a level screw propelling mechanism and a discharging device, which can achieve the continuous operation, the equipment is simple, energy saving and reducing consumption, it can realize continuous production.
NOVELTY - The process comprises: decomposing a biomass derivative to produce a gaseous product with less than 0.5 wt.% of coke precursors and 1 wt.% of gaseous hydrogen; and directly introducing the gaseous product into a steam reformer. The step of decomposing of the biomass derivative is carried out at 200-350 degrees C and pressure of greater than 101.3 kPa.    USE - The process is useful for producing renewable hydrogen, which is useful: as a feedstock for the manufacture of chemicals; as a clean fuel in combustion engines; for manufacture of fertilizers; for petroleum processing and methanol synthesis; for production of chemicals and fuels; for annealing of metals and producing electronic materials; and for domestic and vehicle applications.    ADVANTAGE - The process is capable of economically producing the renewable hydrogen in an eco-friendly manner.
NOVELTY - The utility model claims a scale pig farm waste water processing system, comprising a biogas tank, grizzly screen well, an adjusting pool, a primary sedimentation tank, an anaerobic tank, a pond, A/O tank, a reaction tank, sedimentation tank and disinfection tank, the marsh gas pool, a grid well, an adjusting pool, a primary sedimentation tank, an anaerobic tank, a pond, A/O tank, a reaction tank, sedimentation tank and disinfection tank according to the order sequence. The processing cost is low, and the processing ability is strong, it is suitable for large-scale pig farm waste water treatment;
NOVELTY - This utility model is a kind of large biomass fixed bed gasification furnace, belonging to the biomass gasification field, comprising a hearth, a fuel uniform distribution plates, a guide rail, an interlayer, a gas outlet pipe, a cylinder, a grid, an ash screw conveyer,. Wherein a biomass entering the hearth from the upper part, the pyrolysis and gasification reaction in the furnace, the generated gas is discharged from the induced draft fan through gas outlet pipe. This utility model combined with biomass fuel gas and biomass gasification, the gasification furnace adopts the special structure to realize high-efficient biomass fuel.
NOVELTY - This utility model is a kind of biomass fuel gas system of steel rolling, belonging to the biomass comprehensive utilization technology field. Mainly comprises a fluidized bed gasification furnace, a gas purifying unit and steel furnace, a fluidized bed gasification furnace through the gas purifying unit and the rolling steel furnace; And in the utility model biomass raw material into the fluidized bed gasification furnace, a bed material carrying the fluidized in the furnace, generating gas by fast pyrolysis and gasification reaction, gasification by air blower through the uniform pressure chamber from the side of said fluidized bed gasification furnace, biomass fuel by dust is directly sent into the rolling steel furnace air distribution combustion by gas nozzle. This utility model can realize biomass into clean fuel gas, high efficiency released heat in the steel rolling furnace and greatly reduces the sulfur dioxide and nitrogen oxide. Produced by gasification of solid emission is plant ash, the whole system is the production process has no tar and sewage discharge.
NOVELTY - This utility model is a kind of biomass gasification drying system, belonging to the biomass comprehensive utilization field, comprising a furnace front storage hopper, a feeding spiral conveyer, gasification furnace hearth, an air distribution plate, air chamber, air inlet, a discharging spiral conveyer, a gas outlet pipe, a cyclone dust collector, the ash discharging spiral conveyer, a hot-blast stove, a drier, a cyclone separator, a draught fan and a chimney. Then it is added into biomass gasification furnace hearth composed of spiral conveyer, the pyrolysis and gasification reaction in the gasification furnace to generate gas dust-removing by cyclone dust collector, a gas is directly sent to the high temperature hot-blast stove combustion providing heat source for drying system. This utility model combined with biomass fuel gas and biomass gasification, a biomass fluidized bed gasification, high temperature gas-solid separation, gas combustion, high temperature flue gas drying technology, the biomass fuel energy for use.
NOVELTY - The utility model claims a hydrogen-oxygen mixed power device, especially relates to a method for generating a cracking tank hydrogen-oxygen mixed gas to the device. Is connected with multiple said electrolytic slot, in the electrolytic tank filled with electrolyte, an electrolytic anode and the electrolysis cathode is set in the electrolyte, wherein the electrolyte contains alcohol, ethylene glycol, organic silicon antifoaming agent and alkali. The electrolytic groove is provided with a first external electric field electrode, a anode close to the electrolytic anode, a cathode close to the electrolysis. In said electrolytic groove provided with a sensor, and a pressure sensor element is arranged between the first upright rod, the liquid level sensing element and a sensing element. This utility model can produce hydrogen and oxygen, cracking process more easy. it is high-efficient and low-energy consumption and ensures the safe work of the water splitting in the work.
NOVELTY - Blast-furnace (1) operation method involves separating carbon dioxide from waste gas of combustion furnace which uses blast furnace gas as portion or all of a fuel, and modifying separated carbon dioxide gas in methane by blowing reducing gas into blast furnace.    USE - Blast-furnace operation method (claimed).    ADVANTAGE - The method enables efficient and economical separation of carbon dioxide, by simple method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating blast furnace method. (Drawing includes non-English language text)    Blast furnace (1)    Hot-blast stove (2)
NOVELTY - A hydrogen generating apparatus (100) comprises reactor (20) which performs reaction related to generation of hydrogen-containing gas using raw material, combustor (5) for heating reactor, taper-shaped combustion exhaust gas flow path (8) through which combustion exhaust gas produced with combustor flows, exit (7) provided in downstream end surface of combustion exhaust gas flow path, and part (22a, 22b) which collides with flow of combustion exhaust gas and is provided in combustion exhaust gas flow path.    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Reactor is uniformly heated, and drift in taper-shaped combustion exhaust gas flow path is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Combustor (5)    Exit (7)    Combustion exhaust gas flow path (8)    Reactor (20)    Part (22a, 22b)    Hydrogen generating apparatus (100)
NOVELTY - The reactor has a reaction chamber (12) is overlapped on lower reaction tank (8). The speed regulation circulating pump (7) is set on the sludge reflux pipe. The sludge reflux pipe is connected with an automatic traction backflow circulating device (3). The feeding tube is provided with a protective cover (2). The biogas residue overflow pipe (15) is provided with a back-flushing switch.    USE - STAIC efficient anaerobic reactor.    ADVANTAGE - The production rate can be improved. The floor space and cost of reactor can be reduced. The blockage of material liquid in the pipeline is prevented. The anti-punching effect of the tank casing can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the STAIC efficient anaerobic reactor.    Protective cover (2)    Automatic traction backflow circulating device (3)    Speed regulation circulating pump (7)    Lower reaction tank (8)    Reaction chamber (12)    Biogas residue overflow pipe (15)
NOVELTY - A sludge biomass fuel comprises biochemical sludge comprising industrial wastewater treated sludge and sewage processed sludge, and plant waste. The plant waste is dry wood, tree bark, chaff, corn core, straw, and peanut shell. The particle diameter of plant waste is not more than 0.7 cm.    USE - Sludge biomass fuel (claimed).    ADVANTAGE - The sludge biomass fuel is economically processed by environmentally-friendly process with reduced energy consumption. The biochemical sludge and plant waste are recycled effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological fermentation.
NOVELTY - This utility model claims a kind of biomass carbonizing gas filtering device, wherein the filtering device comprises a cavity and a cavity, wherein the cavity comprises a base, a bottom plate, a cylinder, an air inlet, a middle flange ring and a tar discharging exit, the upper cavity comprises an upper cylinder body, filter cylinder, the end flange, the top cover, an exhaust port and a sealing ring. The beneficial effect of the utility model is a filter tank is simple in structure, ((/lu:xiao)), and maintenance is convenient to clean, the combustion gas further purification, ensures the good operation of the fan.
NOVELTY - Manufacture of synthesis gas from wood wastes involves drying wood wastes, heating, steam modifying at 700-1000 degrees C and pyrolyzing at 250-650 degrees C such that charcoal is formed.    USE - Manufacture of synthesis gas from wood wastes (claimed).
NOVELTY - A nitrogen-containing product is obtained by combining polymeric material and chemical reagent in a reactor, and heating the resultant product at 20-250 degrees C. The chemical reagent is obtained by combining nucleophilic agent and electrophilic agent.    USE - Nitrogen-containing product is used for conditioning soil, fertilizing soil, tinting or coloring material, recreational field, agricultural field, cement, battery and capacitor (all claimed).    ADVANTAGE - The environmentally-friendly nitrogen-containing product is economically manufactured.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of nitrogen-containing product;    (2) method of tinting or coloring material, which involves mixing material with the nitrogen-containing product; and    (3) method of filtering aqueous or nonaqueous stream, which involves mixing aqueous or nonaqueous stream with nitrogen-containing product.
NOVELTY - Straw coal fuel prepared by crushing raw material into powder according to proportion to obtain the product, performing physical carbonization on the product at normal temperature for 6-8 hours and leveling the product using a shaping pressing mechanism.    USE - Used as straw coal fuel.    ADVANTAGE - The straw coal fuel can be prepared with large proportion, convenient storage and transportation and natural raw materials, and without chemical components.
NOVELTY - Esterification of biodiesel, comprises adding waste oil in a reaction kettle, adding phosphoric acid as catalyst, performing esterification reaction at a temperature of 150-155 degrees C under a reaction pressure of 0.8-0.85 MPa using a homogeneous system.    USE - The method is useful for esterification of bio-diesel (claimed).    ADVANTAGE - The method performs esterification on biodiesel with high conversion rate of the traditional technique 90-95% and breakthrough reaches more than 99.5% in a short time consuming manner.
NOVELTY - Methane is produced by hydrogasification of heavy petroleum residues at low temperature (300-350 degrees C) and pressure (30-35 atm), in the presence of a catalyst. The ratio of catalyst and feedstock is 0.5:1. The catalyst comprises highly dispersed Raney nickel with aluminum hydroxide carrier.    USE - Production of methane (claimed).
NOVELTY - The method comprises subjecting organic substrates containing fertilizers, gaseous energy carrier and industrial water to a preliminary aerobic processing unit, heating the substrates to form oxygen gaseous products, subjecting the heated substrate to a secondary anaerobic processing unit to obtain biogas and processed substrate, and separating the substrate into liquid fractions containing oxygen gaseous products and condensed fraction containing fertilizers.    USE - The method is useful for biologically processing concentrated organic substrates such as effluents (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for biological processing concentrated organic substrates.
NOVELTY - Making esters of glycerin from glycerin containing by-product for manufacturing biodiesel fuel on the basis of the renewed plant feedstock, involves after vacuum distillation of residual methanol using 70-90 wt.% glycerin, subjecting glycerin containing product to intermolecular dehydration at 130-150 degrees C, preferably 130-140 degrees C and at a residual pressure of 20-25 mm Hg, to obtain mono-esters or di-esters of glycerin.    USE - For making esters of glycerin which are used in manufacturing biodiesel fuel and gasoline (claimed).    ADVANTAGE - The obtained esters of glycerin is suitable for manufacturing biodiesel fuel on the basis of the renewed plant feedstock.
NOVELTY - A liquid perfume article contains two or more immiscible phases of different color.    USE - Liquid perfume article (claimed).
NOVELTY - The system has a steam reformer (20) which performs steam reforming of the natural gas using water, and generates reformed gas. A methanol synthesis tower (30) synthesizes the methanol from reformed gas. A petrol synthesis tower (50) generates petrol and water from the synthesized methanol. A water recovery line (61) supplies the water to steam reformer in order to utilize the steam reforming of natural gas. A carbon dioxide recovery apparatus recovers carbon dioxide from the waste gas emitted with steam reformer. The line supplies the recovered carbon dioxide to the steam reformer.    USE - System for manufacturing petrol through methanol from natural gas.    ADVANTAGE - The combination of petrol can be utilized effectively. The water vapor required for large quantity can be covered with reusing the water generated on the occasion of petrol synthesis to the steam reforming of natural gas. The production places of natural gas are desert and the ocean in many cases, and for obtaining the fresh water which can be used for steam reforming. The water which can be used for steam reforming can be easily covered with system inside.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing petrol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for manufacturing petrol. (Drawing includes non-English language text)    Boiler (10)    Steam reformer (20)    Methanol synthesis tower (30)    Petrol synthesis tower (50)    Water recovery line (61)
NOVELTY - Producing biogas from processing residues of fruits, beets or tubers or from unprocessed fruits, beets or tubers as starting substrate, which is to be fermented in a biogas reactor, comprises supplying a process auxiliary agent during the drop of minimum value of the ammonium-nitrogen concentration into the fermentation substrate. The process auxiliary agent does not form biogas. The process auxiliary agent comprises a substance, which is released into the fermentation substrate by deamination of ammonium nitrogen.    USE - The method is useful for producing biogas from processing residues of fruits, beets or tubers or from unprocessed fruits, beets or tubers.
NOVELTY - Method for regeneration of carbon-based solid acid catalyst involves performing sulfonation process by placing used carbon-based solid acid catalyst in sulfuric acid through solubilizate process.    USE - Method for regeneration of carbon-based solid acid catalyst used for saccharification of biomass.    ADVANTAGE - The method efficiently enables regeneration of carbon-based solid acid catalyst by economical process with reduced consumption of energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid-acid catalyst regeneration apparatus (3A).    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of regeneration apparatus. (Drawing includes non-English language text)    Solid acid catalyst regeneration apparatus (3A)    Reaction tube (3a)    Sulfuric acid tank (3d)    Sulfuric acid feed pump (3e)    Sulfuric acid supply valve (3f)
NOVELTY - The apparatus (1) has a modifier (2) which generates reformed gas with hydrogen. A temperature detector (9) detects temperature of modifier. A combustor (3) supplies heat to modifier for burning reformed gas. A flame detector (10) detects ionic current value of flame obtained from the combustor. A material supply device (4) supplies raw material to the modifier. A controller (8) controls flow volume of raw material supplied from the material supply device when detected temperature of modifier and ionic current value of flame are set in the predetermined value.    USE - Hydrogen generating apparatus of fuel cell system (claimed) such as polymer electrolyte fuel cell system and solid oxide fuel cell system for mobile object.    ADVANTAGE - The occurrence of abnormality in temperature detector can be detected effectively, since controller is provided to control flow volume of raw material supplied from the material supply device when detected temperature of modifier and ionic current value of flame are set in the predetermined value. The power generation characteristic of fuel cell can be improved efficiently by reducing concentration of unreacted hydrocarbon contained in reformed gas discharged from the hydrogen generating apparatus. The deterioration of catalyst can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system.    Hydrogen generating apparatus (1)    Modifier (2)    Combustor (3)    Material supply device (4)    Controller (8)    Temperature detector (9)    Flame detector (10)
NOVELTY - The hydrogen production apparatus (50) has a hydrogen gas exhaust passage (5) which discharges exhaust gas and floating water droplet (6) comprising solute and hydrogen from a hydrogen generation unit (1) to water or hydrogen gas. The hydrogen generation unit generates aqueous solution (8). The exhaust gas circulated in the hydrogen gas exhaust passage is flowed in a solute removal unit (3). The floating water droplet is removed from the exhaust gas by the solute removal unit.    USE - Hydrogen production apparatus used in electric power generating apparatus (claimed).    ADVANTAGE - Since the solute removal unit can remove the floating water droplet from the exhaust gas, the floating water droplet with the solute can be easily removed from the hydrogen gas manufactured by the hydrogen generation unit by the solute removal unit. Hence the bad influence to the hydrogen production apparatus by the solutes can be prevented. Since the hydrogen gas manufactured with the hydrogen production apparatus can be used for the fuel gas of the direct fuel cell, the storage of the hydrogen gas can be eliminated, and the size of the electric power generating apparatus can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electric power generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen production apparatus. (Drawing includes non-English language text)    Hydrogen generation unit (1)    Solute removal unit (3)    Hydrogen gas exhaust passage (5)    Floating water droplet (6)    Aqueous solution (8)    Hydrogen production apparatus (50)
NOVELTY - The system has a collection part (10) attached to a cooling unit (9) that cools naphtha gas component discharged from a low temperature fractionating column (7). A temperature control unit (P2) controls temperature of a high temperature fractionating column (6) for supplying cracked distillate of light oil collected through a supply line (L3). Another temperature control unit (P3) controls the temperature of the low temperature fractionating column for supplying naphtha fraction recovered by the collection part through another supply line (L4) to the low temperature column.    USE - System for manufacturing bio-diesel fuel. Uses include but are not limited to waste edible oil, plant derived fat/oil, model system fat/oil and mineral oil.    ADVANTAGE - The temperature control unit controls the temperature of the low temperature column for supplying naphtha fraction recovered by another collection part through the supply line to the low temperature column, so that local temperature irregularity is reduced, thus realizing temperature-control quickly with respect to a solid catalyst reactor or load fluctuation of hydrocarbon oil vapor, and improving fractional-distillation precision and light oil yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a diesel-fuel manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a diesel-fuel manufacturing system.'(Drawing includes non-English language text)'    Supply lines (L3, L4)    Temperature control units (P2, P3)    High temperature fractionating column (6)    Low temperature fractionating column (7)    Collection parts (8, 10)    Cooling unit (9)
NOVELTY - The method involves filling a hydrogenation catalyst, and providing bio-oil and hydrogen as a raw material. A hydrogenation process is performed in a hydrogenation reactor by reducing an active component of the hydrogenation catalyst. A hydrogenation effluent circulation is performed in a first reaction area. A hydro-refining operation is performed, and the refining catalyst is filled in a second reaction area. A gas phase circulation is performed in a third reaction area by distillation of naphtha and ultra-low-sulfur to obtain low freezing point diesel oil.    USE - Method for selectively hydrogenating and producing high quality diesel oil.    ADVANTAGE - The method enables improving storage stability of the fuel oil, so that the production efficiency of low-solidifying clean diesel oil can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for selectively hydrogenating and producing high quality diesel oil. '(Drawing includes non-English language text)'
NOVELTY - The method involves filling a hydrogenation catalyst, and providing bio-oil and hydrogen as a raw material. A hydrogenation process is performed in a hydrogenation reactor by reducing an active component of the hydrogenation catalyst. A hydrogenation effluent circulation is performed in a first reaction area. A hydro-refining operation is performed, and the refining catalyst is filled in a second reaction area. A gas phase circulation is performed in a third reaction area by distillation of naphtha and ultra-low-sulfur to obtain low freezing point diesel oil.    USE - Method for selectively hydrogenating and producing low solidifying point bio-diesel.    ADVANTAGE - The method enables improving storage stability of the fuel oil, so that the production efficiency of low-solidifying clean diesel oil can be improved.    DETAILED DESCRIPTION - The bio-oil is selected from any of vegetable oil or animal fat.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for selectively hydrogenating and producing low solidifying point bio-diesel. '(Drawing includes non-English language text)'
NOVELTY - The method involves filling a hydrogenation catalyst, and providing bio-oil and hydrogen as a raw material. A hydrogenation process is performed in a hydrogenation reactor by reducing an active component of the hydrogenation catalyst. A hydrogenation effluent circulation is performed in a first reaction area. A hydro-refining operation is performed, and the refining catalyst is filled in a second reaction area. A gas phase circulation is performed in a third reaction area by distillation of naphtha and ultra-low-sulfur to obtain low freezing point diesel oil.    USE - Method for selectively hydrogenating and producing low solidifying point bio-diesel.    ADVANTAGE - The method enables improving storage stability of the fuel oil, so that the production efficiency of low-solidifying clean diesel oil can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for selectively hydrogenating and producing low solidifying point bio-diesel. '(Drawing includes non-English language text)'
NOVELTY - This utility model claims a kind of using solar energy and marsh gas to heating the constant temperature anaerobic sewage treatment system. Is composed of a fermentation tank, a heating system, wherein the fermentation tank body is cylindrical, the bottom is equipped with a plate, the fermentation tank top cover with a special marsh gas top film, a fermenting tank outer wall of heating coil pipe, the outer wall heating coil pipe is provided with a circulating water, a heating system comprises a solar heat collecting system, a solar heating system and a methane heating system, wherein the solar heat collecting system is composed of a solar energy vacuum heat collector, a solar vacuum heat collector and water tank, the water tank is connected with the heating coil pipe of a tank, a marsh gas heating system and the outer wall heating coil; Using the hot water in the solar energy photo-thermal system, a circulating flow anaerobic fermentation tank outer wall of the coil to reach to the pool wall. Under the condition of low temperature, is generated by combusting the marsh gas anaerobic tank, heating circulating water, a stable complete solar water heating system to ensure the single sewage treatment system;
NOVELTY - Laundry detergent composition comprises 5-15 wt.%, preferably 10 wt.% anhydrous lanolin; 5-15 wt.%, preferably 10 wt.% nitromethane; 30-40 wt.%, preferably 35 wt.% difluorotetrachloroethane; 40-60 wt.%, preferably 50 wt.% butane; 2-10 wt.%, preferably 6 wt.% isopropyl alcohol; and 2-6 wt.%, preferably 4 wt.% water.    USE - As laundry detergent composition useful for cleaning fur clothes (claimed).    ADVANTAGE - The present composition has rational prescription, is convenient to use, when sprayed on the fur surface, dirt can be easily wiped out by using wet and soft cloth; effective for removing stain; and it does not hurt skin.
NOVELTY - This utility model claims a double-stage double-cyclic anaerobic reactor, comprising a main body, wherein the bottom of the main body further comprises a water inlet water distribution device, the first level three phase separator and a level three phase separator body from top to bottom in turn is divided into a deposition depth evolution reaction chamber and reaction chamber, the first level three phase separator by a one-stage biogas lift pipe gas-liquid separator is connected with the first level, the first level gas-liquid separator is connected with a first grade marsh gas exhaust pipe and the secondary gas-liquid separator, a gas-liquid separator is connected with a secondary marsh gas riser and a level three phase separator, a gas-liquid separator for air outlet extend out the body, the first grade gas-liquid separator and the secondary gas-liquid separator is respectively connected with the circulation loop. This utility model is used for carrying out the high-efficient anaerobic biological treatment of waste water, high volume load, saves investment and floor area, an inner circulation flow is big, save power consumption, and has outer circulation, anti-impact load resistance, water stability, and it can be recycled.
NOVELTY - The apparatus (1) has desulfurization unit (5) that removes sulfur component from feed gas. Evaporation passage (8) heats desulfurized gas and reforming water to obtain mixed gas from which modification unit (3) yields hydrogenous gas. High-temperature transformation unit (6a) lowers carbon monoxide concentration in hydrogenous gas. Desulfurization unit communicates with reforming unit by evaporation passage. Transformation unit is arranged over desulfurization unit along evaporation passage to communicate modification unit and low-temperature transformation unit (6b).    USE - Fuel treating apparatus used for producing hydrogen supplied to fuel cell system such as home-use cogeneration system.    ADVANTAGE - The fuel treating apparatus with the high reaction efficiency of a catalyst and with small influence of the temperature from an external environment is provided. Since piping for connection of fuel treating apparatus and external apparatus is arranged at the bottom and side surface of the fuel treating apparatus, each component does not interfere with each other while assembling the apparatus and the fuel treating apparatus can be manufactured easily. Since the active efficiency of the reaction catalyst is uniformly maintainable according to the fuel treating apparatus, the improvement of the reliability of apparatus can be attained. Since thickness of the heat insulating material which prevents thermal radiation and arranged on the outer periphery of apparatus can be made thinner, the apparatus can be reduced in size.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel treating apparatus. (Drawing includes non-English language text)    Fuel treating apparatus (1)    Modification unit (3)    Desulfurization unit (5)    High-temperature transformation unit (6a)    Low-temperature transformation unit (6b)    Evaporation passage (8)
NOVELTY - Increasing the potential of the production of biofuel from microalgae comprises growing the selected microalgae in a cultured medium enriched with a first bio-modulator and exposed to light, performing stress step by increasing the salinity of the medium using a second bio-modulator, and passively recovering the biomass by ad hoc changing pH values of the culture medium using a third bio-modulator.    USE - The method is useful for increasing the potential of the production of biofuel from microalgae in the production of molecules such as carotenoids and polyunsaturated fatty acids with high added value, where the microalgae: are salt-tolerant species and/or classes of Chlorophyceae, Cyanophyceae, Bacillariophyceae, Xanthophyceae and Chrysophyceae; and belong to Dunaliella tertiolecta (preferred), Chlorella, Nannochloropsis, Haematococcus, Skeletonema, Melosira, Thalassiosira, Nitzschia and Navicula (all claimed).    ADVANTAGE - The method energy efficiently, rapidly and passively recovers the biomass without the step of centrifugation or filtration, and ensures very selective cultivation requirements thus reducing the risks of contamination by other microalgae, bacteria or fungi.
NOVELTY - Process for production of biogas from organic material, involves treating organic material with an enzyme composition comprising a phytase, and digesting the enzyme treated organic material to form biogas.    USE - The process is useful for production of biogas from organic material (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of an enzyme composition comprising phytase (a) to increase the digestibility of proteins and polysaccharides by microbes present in a process suitable for the conversion of organic material into biogas, (b) to increase the availability of minerals in a process suitable for the conversion of organic material into biogas or (c) to reduce precipitation of salts on hardware such as (metal) surfaces and in lines and pumps in a process suitable for the conversion of organic material into biogas.
NOVELTY - Converting pyrolysis oil and crude tall oil involves subjecting pyrolysis oil to one or more pretreatments steps selected from treatment with an aqueous media, high temperature high pressure treatment (HTHP), prehydrogenation, and extraction, and its combinations to obtain pretreated pyrolysis oil, and subjecting feed comprising pretreated pyrolysis oil and crude tall oil to hydroprocessing under hydroprocessing conditions in the presence of hydrogen and hydroprocessing catalyst where an effluent comprising hydrocarbons boiling in the liquid fuel hydrocarbon range is obtained.    USE - The process is useful for converting pyrolysis oil and crude tall oil (claimed).    ADVANTAGE - Process is provided for effectively and economically processing feed comprising pyrolysis oil originating from biomass and crude tall oil, to provide more valuable components, particularly to provide liquid fuels, suitably transportation fuels and blending components for the fuels, as well as heating oil, solvents, fine chemicals and chemical building-blocks. Thermally stable and fungible liquid fuels are also provided based at least partly on renewable starting materials, where the fuels are carbon dioxide (CO2) neutral and contain only very low amounts of bonded sulfur and nitrogen, if any.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a product obtainable by the process.
NOVELTY - Composite membrane comprises: a porous support (1); a gutter layer (2), a portion of which is present within the support (2b) and a portion of which is outside of the support (2a); and a discriminating layer (3) on the gutter layer, where the portion of the gutter layer (a1) outside of the support has an average thickness (GLe) of 10-900 nm and (b1) present within the support has average thickness (GLi) of 10- 350% GLe.    USE - The membrane is useful for separation of gases comprising carbon dioxide and methane, and refining methane from biogas and in gas separation module (all claimed).    ADVANTAGE - The composite membrane has: pure water permeability of less than 6.10-8 m3/m2.s.kPa, preferably less than 3.10-8 m3/m2.s.kPa at 20 degrees C; dry thickness of 20-500 mu m, preferably 30-300 mu m; and carbon dioxide/methane selectivity ( alpha carbon dioxide/methane) of greater than 20, and carbon dioxide/nitrogen selectivity ( alpha carbon dioxide/nitrogen) of greater than 35. The composite membrane: exhibits good flux and separation selectivity (they can endure bending and have a low tendency to form undesirable pin holes); and is stable under variety of conditions, including hot and humid conditions.    DESCRIPTION OF DRAWING(S) - The figure illustrates schematic view of the composite membrane.    Porous support (1)    Gutter layer (2)    Portion of the gutter layer outside of the support (2a)    Portion of the gutter layer within the support (2b)    Thin discriminating layer (3)
NOVELTY - One pot process for preparing saxagliptin monohydrate comprises (a) reacting saxagliptin salt compound (III) with a base to form a reaction mixture containing a (3S)-2-(2-aminoacetyl)-2-azabicyclo(3.1.0)hexane-3-carbonitrile compound (IV), (b) adding greater than 4 molar equivalent of water with (IV) to the reaction mixture obtained in step (a) in-situ, and (c) isolating saxagliptin monohydrate.    USE - The process is useful for preparing saxagliptin monohydrate (claimed), which is useful for improving glycemic control in patient with type 2 diabetes mellitus. No biological data given.    ADVANTAGE - The improved one pot process provides saxagliptin monohydrate, with high yield and high purity (greater than 99%), improved reproducibility, and reduced manufacturing cost in a simple and environmentally friendly manner, thus avoiding the formation of isomeric and other process related impurities.    DETAILED DESCRIPTION - One pot process for preparing saxagliptin monohydrate comprises (a) reacting saxagliptin salt compound of formula (III) with a base to form a reaction mixture containing a (3S)-2-(2-aminoacetyl)-2-azabicyclo(3.1.0)hexane-3-carbonitrile compound of formula (IV), (b) adding greater than 4 molar equivalent of water with (IV) to the reaction mixture obtained in step (a) in-situ, and (c) isolating saxagliptin monohydrate.    HX = acid addition salt.    An INDEPENDENT CLAIM is included for use of trifluoroacetate salt of saxagliptin for the direct preparation of saxagliptin monohydrate.
NOVELTY - A refrigerant mixture either comprises 85-89 wt.% of propane and 11-15 wt.% of propene; or comprises 45-55 wt.% of propane, 5-11 wt.% of propene, and greater than 36 wt.% of butane.    USE - As refrigerant mixture for a refrigeration system such as air conditioning system (all claimed), used in household refrigeration, commercial refrigeration, freezer units, air conditioning units, and heat pumps.    ADVANTAGE - The refrigerant mixture provides increased moisture reduction of 20%, preferably greater than 25%, in a target environment as compared to standard chlorodifluoromethane (R-22) refrigerant mixtures. The mixture is environmentally friendly; offers greater operating efficiency; and has maximum efficiency as drop-in replacement for chlorofluorocarbon (CFC) refrigerants. By using the mixture, unwanted halocarbons can be virtually eliminated and/or significantly diminished while gaining unexpected power efficiencies and moisture removal. Moreover, the hydrocarbon replacement in refrigerant systems can be implemented by drop in replacement in existing system, and dangers associated with use of hydrocarbons can be removed or reduced by exhausting any hydrocarbon leakage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of retrofitting a refrigeration system with a drop-in replacement refrigeration mixture involving replacing at least a portion of a halocarbon refrigerant with an all hydrocarbon mixture comprising 85-89 wt.% of propane and 11-15 wt.% of propene; and    (2) method of recharging a refrigeration system with a drop-in replacement refrigeration mixture comprising 45-55 wt.% of propane, 5-11 wt.% of propene, and greater than 36 wt.% of butane.
NOVELTY - The methane obtaining device has a column that is installed in center of main container with areas for fastening by cable system and is made from elastic material. A wooden flooring is installed to divide basic containers and gas holder. A system of removal of mechanical impurities, a system of filtration and removing water from biogas, the line of the withdrawal of filtered gas, underground drainage controller, the line of withdrawal of purified gas, the line of withdrawal of condensate and automated control system are arranged under the wooden flooring.    USE - Device for obtaining methane during processing of biomass.
NOVELTY - A long chain alkane with carbon number of 6-24 is converted by mixing glycerol and 5-50 wt.% aqueous inorganic acid solution with molar ratio of 1-2, adding catalyst in which carrier has metal main catalyst which is iridium (Ir) or rhodium (Rh) and metal co-catalyst which is rhenium (Re), tungsten (W), and/or molybdenum (Mo) with concentration of 1-3 wt.% and weight ratio of 0.5-5 in the presence of pressurized hydrogen, and stirring at 120-350 degrees C.    USE - Catalytic conversion of long chain alkane (claimed).    ADVANTAGE - Process is simple, has mild reaction condition, low equipment requirements, and low cost, solves problem in conversion of glycerol in biodiesel production, and provides effective way of regenerating fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst which involves mixing 0.012-0.024 g metal main catalyst precursor which is chloroiridic acid (H2IrCl6) or rhodium(III) chloride (RhCl3) and 0.01-0.036 g metal co-catalyst precursor which is potassium perrhenate (KReO4), ammonium phosphomolybdate trihydrate, and/or phosphotungstic acid, dissolving 0.4 g of carrier in 5 ml deionized water, heating and stirring to obtain catalyst precursor, drying in oven, drying in tube furnace at room temperature to 300 degrees C at rate of 2 degrees C/minute, calcining, adding 5 ml deionized water into high-pressure autoclave with magnetic stirrer at 180-300 degrees C and hydrogen pressure of 6-10 MPa, and replacing air in autoclave with hydrogen gas.
NOVELTY - Impurities are removed from natural gas by introducing natural gas to tubular heating furnace at 800-1200 degrees C for thermal decomposition in which length of heating zone of tubular heating furnace is 0.5-3 m, and gas flow rate is 0.1-5 L/minute, and removing solid impurities.    USE - Removing impurities i.e. phosphorus, borane, arsine, and hydrogen sulfide gas in natural gas.    ADVANTAGE - Removal method is simple and energy-saving, has high gas cleaning efficiency, eliminates use of adsorbents, and does not create new impurities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device comprising tubular heating furnace (3) connected to dust collector (4) at one end.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a device for removing gas impurities in natural gas.    Flowmeter (1)    Pre-heater (2)    Tubular heating furnace (3)    Dust collector (4)    Dust collector filter (5)
NOVELTY - An input torch with oxygen-mixed combustion-enhanced hydrocarbons comprises hydrocarbon base gas and 0.05-4.5 wt.% energy efficient additive composite in which hydrocarbon is compound of formula C1-4H2-10 or 4-12 carbon-containing complex and hydrocarbon base gas total amount is 100 wt.% and energy efficient additive composite contains 0.1-0.5 wt.% organometallic compound, 5-14 wt.% carbon disulfide, 12-21 wt.% ethyl nitrile or ethyl nitrate, 36-51 wt.% heterocyclic ether compound, 6-17 wt.% nitrogen-containing compound, and 3-12 wt.% alicyclic compound.    USE - Input torch with oxygen-mixed combustion-enhanced hydrocarbons for thermal metal cutting, machining, welding, preheating, and perforation.    ADVANTAGE - The input torch is low cost, residue-free, and safe, improves and optimizes flame temperature performance, and reduces flash point, fuel burning rate, oxygen consumption, and black smoke.    DETAILED DESCRIPTION - An input torch with oxygen comprises hydrocarbon base gas and 0.05-4.5 wt.% energy efficient additive composite in which hydrocarbon in base gas is compound of formula C1-4H2-10 or 4-12 carbon-containing complex and hydrocarbon base gas total amount is 100 wt.%, energy efficient additive composite contains 0.1-0.5 wt.% organometallic compound, 5-14 wt.% carbon disulfide, 12-21 wt.% ethyl nitrile or ethyl nitrate, 36-51 wt.% heterocyclic ether compound, 6-17 wt.% nitrogen-containing compound, and 3-12 wt.% alicyclic compound with respect to total of 100 wt.%, organometallic compound is cyclopentadienyl iron or barium sulfonate alkyl, heterocyclic ether compound is 1,4-epoxybutane, ethylene oxide, and diethyl ether, nitrogen-containing compound is ethylamine, diethylamine, triethylamine, trinitromethane, methylamine, dimethylamine, and trimethylamine, and alicyclic compound is cyclopentene, cyclopentadiene, and cyclohexene.
NOVELTY - Forestry environmental-friendly pesticide comprises 1-3 pts. wt. Metarrhizium anisopliae powder, 2-4 pts. wt. Hirsutella thompsonii powder, 0.3-0.5 pts. wt. Aschersonia powder, 1-3 pts. wt. caterpillar fungus powder, 3-6 pts. wt. sea-tangle, 1-2 pts. wt. rhizoma anemarrhenae, 0.1-0.2 pts. wt. frankincense, 1-4 pts. wt. fortune eupatorium herb, 2-8 pts. wt. rhizoma cibotii, 3-6 pts. wt. herba lycopi, 4-7 pts. wt. rhizoma alismatis, 2-4 pts. wt. Rhodococcus powder, 23-34 pts. wt. Alocasia, 11-19 pts. wt. hemlock and 1-16 pts. wt. Gelsemium    USE - Used as a forestry environmental-friendly pesticide.    ADVANTAGE - The pesticide is environmental-friendly (claimed) and highly efficient; does not produce secondary toxicity, residue and pollution; and maintains ecological balance.    DETAILED DESCRIPTION - Forestry environmental-friendly pesticide comprises 1-3 pts. wt. Metarrhizium anisopliae powder, 2-4 pts. wt. Hirsutella thompsonii powder, 0.3-0.5 pts. wt. Aschersonia powder, 1-3 pts. wt. caterpillar fungus powder, 3-6 pts. wt. sea-tangle, 1-2 pts. wt. rhizoma anemarrhenae, 0.1-0.2 pts. wt. frankincense, 1-4 pts. wt. fortune eupatorium herb, 2-8 pts. wt. rhizoma cibotii, 3-6 pts. wt. herba lycopi, 4-7 pts. wt. rhizoma alismatis, 2-4 pts. wt. Rhodococcus powder, 23-34 pts. wt. Alocasia, 11-19 pts. wt. hemlock, 1-16 pts. wt. Gelsemium, 2-3 pts. wt. flower tree powder, 5-18 pts. wt. Andrographis herb and 100 pts. wt. water.
NOVELTY - Non-polluting forestry pesticide comprises Metarrhizium anisopliae powder, bacteriophage powder, Bacillus thuringiensis powder, cordate houttuynia, chinaberry seed, tortoise plastron, Notopterygium root, Polygala tenuifolia, fructus forsythiae, root of straight ladybell, wingnut, pepper, synergistic agent, stemona, Chinaberry, camphor, emulsifier, synergistic agent, cordate houttuynia, common andrographis herb, and water.    USE - Used as a non-polluting forestry pesticide.    ADVANTAGE - The pesticide is highly efficient, does not produce secondary toxicity and residue, and maintains ecological balance.    DETAILED DESCRIPTION - Non-polluting forestry pesticide comprises 1-3 pts. Metarrhizium anisopliae powder, 5-6 pts. bacteriophage powder, 2-4 pts. Bacillus thuringiensis powder, 1-6 pts. cordate houttuynia, 4-9 pts. chinaberry seed, 1-6 pts. tortoise plastron, 7-11 pts. Notopterygium root, 2-9 pts. Polygala tenuifolia, 5-8 pts. fructus forsythiae, 4-7 pts. root of straight ladybell, 3-5 pts. wingnut, 11-24 pts. pepper, 1-10 pts. synergistic agent, 10-20 pts. stemona, 15-20 pts. Chinaberry, 4-10 pts. camphor, 3-4 pts. emulsifier, 1-10 pts. synergistic agent, 12-18 pts. cordate houttuynia, 5-18 pts. common andrographis herb, and 100 pts. water.
NOVELTY - Synthesis gas slurry state bed sulfur-resisting methanation catalyst comprises main catalyst metal W' as active component, and W1 metal as auxiliary agent at mass ratio of 1-60:0.5-40.    USE - Synthesis gas slurry state bed sulfur-resisting methanation catalyst.    ADVANTAGE - The catalyst has higher catalytic activity, long service life and high selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of synthesis gas slurry state bed methanation comprising: (A) stirring at 15-60 degrees C at stirring speed of 30-300 revolutions per minute (rpm), preparing catalyst main metal and soluble salt auxiliary metal soluble salt solution, stirring solution for 2-36 hours, standing for 1-12 hours, evaporating solvent at temperature 50-90 degrees C to form viscous solution; (B) drying viscous solution at 70-150 degrees C for 4-36 hours, grinding dried product to 40-200 mesh, roasting at 350-600 degrees C for 1-8 hours to obtain W'-W1 precursor; (C) hydrogen reducing W-W1 precursor at volume ratio of 5-25% in 75-95% nitrogen (N2) mixed atmosphere, where flow speed is 50-200 ml/minute, increasing temperature at rate of 0.5-10 degrees C from room temperature to 350 degrees C, increasing at rate of 0.5-5 degrees C, increasing to 450-700 degrees C, constant temperature reducing for 1-12 hours; and (D) heating, closing hydrogen (H2), and cooling material to room temperature in N2 atmosphere; and    (2) slurry bubble column methanation process reaction condition comprising carrying out reaction at 250-340 degrees C and 1-7 MPa, raw material air hydrogen carbon mol ratio H2/carbon monoxide and carbon dioxide is 1.0-4.0, raw material gas containing sulfur volume percentage is 0.5-7%, and volume space velocity is 600-7000.
NOVELTY - Method for recycling mixed fuel involves injecting mixed fuel containing methanol and gasoline to three adsorption towers comprising adsorbents, placed in series for absorbing and recycling, steam washing, sweeping, cooling, obtaining condensed liquid containing gasoline and water, obtaining gasoline by performing oil-water separation and recycling water for cooling adsorption tower.    USE - Method for recycling mixed fuel (claimed).    ADVANTAGE - The method efficiently enables recycling of mixed fuel by environmentally-friendly process with high gasoline recovery rate.
NOVELTY - A methanol fuel comprises 94-98 wt.% methanol and 2-6 wt.% additives. The additives comprise 20-40 wt.% biodiesel, 20-30 wt.% acetone, 10-30 wt.% ethyl acetate, 5-30 wt.% methylal and 10-20 wt.% turpentine.    USE - Methanol fuel is used for vehicle.    ADVANTAGE - The vehicle using the methanol fuel has excellent fastness, abrasion resistance with respect to movable component, and reduced oil consumption.
NOVELTY - A kind of city sludge pyrolysis device, belonging to the field of solid waste treatment technology, a pyrolysis furnace feeding port is connected with the spiral feeder, the bottom is pyrolytic carbon outlet, the upper part of the separator is connected with the separator ports connected with the liquid storage tank, separator is connected with the condenser, the condenser is connected with the liquid storage tank, a condenser non-condensing gas outlet of the pyrolysis furnace air inlet connected with the pyrolysis furnace return pipe with the pyrolysis furnace of the burner connected with the pyrolysis furnace smoke gas outlet of the spray tower, a fog-removing device, an active carbon adsorption bed. The advantages of the utility model are as: under the oxygen-free condition to heat the sludge, the organic matter thermal cracking and thermal chemical decomposition in the sludge, a generation of dioxins substance and so on harmful gas, pyrolysis gas and hot electrolyte as the energy supply of the pyrolysis, and forming the pyrolytic carbon is used as sewage, waste gas treatment, does not need extra energy or energy is less, at the same time of sewage and processing a raw material.
NOVELTY - This utility model claims an LED photocatalytic hydrogen production device, for packaging LED chip on the package substrate, and a transparent colloid is packaged LED light source and the deposition with photo transparent material bonding the ceramic substrate as a whole so as to make the light emitted by the LED chip can be irradiated to the photo material on the transparent ceramic substrate. At last using sputtering method is plated with insulated waterproof thin film in the electrode, which makes the device is provided with waterproof property, and the device into water to make the material absorb photon generated electron hole pair to make the water into hydrogen.
NOVELTY - The reactor has a spiral feeding unit connected with a storage bin. A pyrolysis reactor main body is provided with a boiler body that is provided with a cracking chamber and a heat storage chamber. Residual biomass material is put into a combustion chamber, where the residual biomass material is heated to generate gas. The heat storage chamber is provided with a rotating device. An annular body is provided with a rotating shaft. The boiler body is connected with a reaction regulator for adjusting a reaction intensity value of the boiler body. A conveying pipeline is passed through a cooler.    USE - Biomass gasification pyrolysis reactor.    ADVANTAGE - The reactor has stable operation and strong adaptability.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a biomass gasification pyrolysis reactor.
NOVELTY - Energy-saving bamboo charcoal firing system comprises a carbonization kettle detachably set inside a furnace of a baking device, a thermometer and an exhaust opening provided at the top of the carbonization kettle. The exhaust opening is connected with a filter through an exhaust pipe inlet. The bottom of the filter is provided with a liquid outlet. The top of the filter is set with a gas pipeline. The gas pipeline is connected with a gas distribution device. The gas distribution device is connected with furnace via a combustion chamber. The air-feeding pipes are set with flow control valve.    USE - Useful as an energy-saving bamboo charcoal firing system.    ADVANTAGE - The system avoids the reprocessing of the fuel, and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for bamboo charcoal firing using the energy-saving bamboo charcoal firing system, comprising (i) adding fuel into the combustion chamber of the furnace, heating the fuel with bamboo in the carbonization kettle at 180-280 degrees C and steaming to obtain bamboo vinegar liquid; (ii) continuously heating the bamboo vinegar liquid for 3.5-4 hours at 650-700 degrees C, heating and distilling the bamboo in the carbonization kettle, discharging the resulting gaseous products from the exhaust opening of the rectifying tower, carrying out gas-liquid separation in the filter to obtain the liquid phase and continuously heating in the gas phase in the carbonization kettle of the furnace; and (iii) introducing the heat generated by the combustion of fuel for carbonization process via the air pipeline, carbonizing for 2 hours at 650-700 degrees C, and sintering to obtain the bamboo charcoal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the energy-saving bamboo charcoal firing system.
NOVELTY - Oxygen and hydrogen oven comprises a microwave oven and electrolysis water.    USE - Used as oxygen and hydrogen oven.    ADVANTAGE - The oxygen and hydrogen oven reduced risk than the conventional ovens, functions without consumption of gas, and adopts semi-permanent stage for electrolysis of copper (1) and zinc (2) in traditional manner (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the oxygen and hydrogen oven.    Copper (1)    Zinc (2)    Hydrogen oxygen concentrator (3)    Power source (5)    Inward current blocking insulator (8)
NOVELTY - The system (100) has water electrolysis stack (1) which produces hydrogen by electrolyzing water. A wet line (32) supplies hydrogen produced by water electrolysis stack to dehumidifying apparatus (31) that adsorbs and eliminates moisture present in hydrogen produced by water electrolysis stack. A compressing device (34) increases pressure of hydrogen in stages, after the elimination of moisture in hydrogen. A purge line (35) takes off some of the hydrogen whose pressure is increased in the compression device, and channels hydrogen to the wet line via dehumidifying device.    USE - Water electrolysis system for supplying hydrogen to hydrogen tank of fuel cell system mounted in vehicle (claimed).    ADVANTAGE - Since the purge hydrogen is not pressure-risen more than necessary, the energy loss can be prevented. The thickness of the purge line can be reduced, so that the leakage of purge hydrogen from the purge line can be prevented. The hydrogen can be reused efficiently, so that the energy loss can be prevented. The hydrogen generating efficiency of the water electrolysis system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis stack (1)    Dehumidifying apparatus (31)    Wet line (32)    Compressing device (34)    Purge line (35)    Water electrolysis system (100)
NOVELTY - Water-rich liquid phase is separated from 3-6C alcohol-rich liquid phase, supplied in a column, to obtain vapor stream comprising water and ethanol. The vapor stream is conducted to rectification column, to obtain liquid distillate comprising water and ethanol, wherein liquid distillate is not reintroduced to the recovery system. Then, 3-6C alcohol is recovered from alcohol-rich liquid phase.    USE - Method for recovering 3-6C alcohol from stream comprising 3-6C alcohol, ethanol and water in recovery system used as biofuel.    ADVANTAGE - The 3-6C alcohol is recovered efficiently from stream comprising 3-6C alcohol, ethanol and water using immiscible properties by simple method by recycling waste stream.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for recovering 3-6C alcohol from stream comprising 3-6C alcohol and water in recovery system;    (2) method for retrofiting ethanol production plant;    (3) dual function column for recovery of 3-6C alcohol;    (4) Composition (A);    (5) Composition (B);    (6) Composition (C);    (7) Composition (D);    (8) Composition (E); and    (9) Composition (F).
NOVELTY - Producing an unsaturated compound comprises subjecting a compound containing 10-24C unsaturated monocarboxylic acids or esters of unsaturated monocarboxylic acids and 4-20C unsaturated dicarboxylic acids or esters of unsaturated dicarboxylic acids to a tandem isomerization/metathesis reaction in presence of a palladium catalyst and a ruthenium catalyst, where the palladium catalyst contains structural element and the catalyst reaction is carried out at less than 3 pKa.    USE - The method is useful for producing unsaturated compound (claimed) i.e. unsaturated alpha , omega dicarboxylic acids and their diesters useful for fuel i.e. metathetisierter biodiesel, plastic applications, surfactants, hydraulic oils and lubricants.    ADVANTAGE - The method enables easily producing the unsaturated compounds from unsaturated monocarboxylic acids and esters of the monocarboxylic acids at very mild temperatures using the palladium or ruthenium catalysts without any chemical activation and without using any solvents.    DETAILED DESCRIPTION - Producing a composition containing an unsaturated compound, comprises subjecting a compound containing 10-24C unsaturated monocarboxylic acids or esters of unsaturated monocarboxylic acids and 4-20C unsaturated dicarboxylic acids or esters of unsaturated dicarboxylic acids to a tandem isomerization/metathesis reaction in presence of a palladium catalyst and a ruthenium catalyst, where the palladium catalyst contains a structural element of formula (Pd-P(R1R2R3)) (I), and is generated in situ, with the proviso that the method is carried out in the absence of substances having a pKa of less than 3.    R1-R3 = 2-10C aliphatic, alicyclic, aryl or heterocyclic, with the proviso that at least one of the radicals R1-R3 is beta -H.
NOVELTY - Propionibacterium freudenreichii KT021 derived from Propionibacterium and isolated from milk deposits using a screening method, is new, where the Propionibacterium freudenreichii is stored in the polish collection of microorganisms under the number of B/00040 in wroclaw.    USE - The Propionibacterium freudenreichii KT021 strain is useful for preparing vitamin B12, propionic acid (all claimed) and folic acid, and is useful for preparing food products, chemicals, biofuels and drugs.
NOVELTY - Obtaining 3-15C, preferably 3-8C higher alcohols, comprises contacting at least one reagent consisting of methanol, ethanol, propanol and isopropanol, and a catalyst, where the catalyst comprises a metal oxide consisting M1 metal including magnesium, zinc, copper, cobalt, manganese, iron, nickel or calcium, and M2 metal including a trivalent gallium, and further contains a noble metal consisting of palladium, platinum, ruthenium, rhodium or rhenium, preferably palladium.    USE - The process is useful for obtaining a 3-15C, preferably 4C higher alcohol such as n-butanol (all claimed), which is useful: for preparing automotive fuels and liquid fuels; and as a starting chemical reagent in plastic industry and an extraction agent in aroma and fragrance industry.    ADVANTAGE - The process rapidly provides 3-15C higher alcohols at low temperature with high yield and improved catalytic activity.
NOVELTY - A composite membrane comprises a porous support (1), a gutter layer (2) and a discriminating layer (3), in which at least 10% of the discriminating layer is intermixed with the gutter layer.    USE - Composite membrane is used for gas separation module for separation of gases e.g. carbon dioxide and methane gases, and refining methane from biogas (all claimed).    ADVANTAGE - The composite membrane has excellent adhesiveness and wettability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of composite membrane.    Porous support (1)    Gutter layer (2)    Discriminating layer (3)    Portions (3a,3b)
NOVELTY - The method involves preparing (S112) cashew nut shell powder by crushing the cashew nut powder and sawdust powder using crusher. The prepared powders are transferred (S121) and stored (S131) to two silos through transfer pipe using pneumatic pressure, respectively. The cashew nut powder and sawdust powder are mixed (S150,S160) into mixing portions through mixer tube. The powders are dried with vortex generated with wing portion formed on screw end. The mixed powders are transferred (S170) to molding unit for compression-molding the mixed powder in pellet form.    USE - Method for manufacturing cashew nut shell component containing timber pellet.    ADVANTAGE - The pellet can be provided with the cashew nut component of the skin and rice hulls or sawdust so that the timber pellet can be effectively replaced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process for manufacturing cashew nut shell component containing pellet. (Drawing includes non-English language text)    Step for preparing cashew nut shell powder (S112)    Step for transferring prepared powders (S121)    Step for storing prepared powders (S131)    Step for mixing powders (S150,S160)    Step for transferring mixed powders to molding unit (S170)
NOVELTY - The method involves preparing (S111,S112) coffee shell powder and rice hulls or sawdust and transferring (S121,S122) them to silos via first transfer pipe. The coffee shell powder and rice hulls or saw dust are stored (S131,S132) in silos and transferred (S141,S142) via second transfer pipe. The coffee shell powder, and rice hulls or saw dusts are mixed (S150,S160) in various mixing portions. The mixture transferred through third transfer pipe is obtained (S170) and compression-molded (S180) with solidity in pellet form. The shaped pellet is cooled and dried (S190).    USE - Manufacturing method of pellet containing coffee shell element and used as fuel.    ADVANTAGE - The pellet with excellent physical property can be manufactured.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the manufacturing method of coffee shell element containing pellet. (Drawing includes non-English language text)    Steps for preparing coffee shell powder and rice hulls or sawdust (S111,S112)    Steps for transferring prepared coffee shell powder and rice hulls or sawdust to silos (S121,S122)    Steps for storing coffee shell powder and rice hulls or sawdust in silos (S131,S132)    Steps for transferring coffee shell powder and rice hulls or sawdust (S141,S142)    Steps for mixing coffee shell powder and rice hulls or sawdust in various mixing portions (S150,S160)    Step for obtaining mixture (S170)    Step for compression-molding mixture (S180)    Step for cooling and drying pellet (S190)
NOVELTY - Composition comprises isolated secreted alpha -xylosidase and at least 5 wt.% cellulase.    USE - The composition is useful for conversion of plant biomass into fermentable sugars (claimed) which are useful for producing biofuels including ethanol.    ADVANTAGE - The composition: reduces the overall cost of biofuel production (expressed as dollars of enzyme needed per liter of fuel); and enhances biomass conversion into free, fermentable sugar residues, and thus provides higher yields of ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) conversion of plant biomass into fermentable sugars, comprising: providing a plant biomass comprising a hemicellulose material, and an enzyme mixture comprising an isolated alpha -xylosidase and a cellulase; and incubating the biomass with the enzyme mixture for a time and under conditions sufficient to create a depolymerized hemicellulose material, where the depolymerized hemicellulose material comprises many free fermentable xylose and glucose residues; and    (2) expressing (M2) alpha -xylosidase comprising culturing a host cell comprising an isolated nucleic encoding an alpha -xylosidase enzyme for a time and under conditions for expression of the alpha -xylosidase enzyme.
NOVELTY - Method of producing ethanol, involves contacting a biomass composition with an enzymatic composition comprising an isolated polypeptide having endoglucanase activity and comprising an amino acid sequence that is at least 90% identical to 230 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, to yield a sugar solution, adding to the sugar solution a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol.    USE - The method is useful for producing ethanol (claimed).    ADVANTAGE - The method enables to provide high yield, and generate stable transformants. The produced ethanol is environmentally-friendly.    DETAILED DESCRIPTION - Method of producing ethanol, involves (a) contacting a biomass composition with an enzymatic composition comprising an isolated polypeptide having endoglucanase activity and comprising an amino acid sequence that is at least 90% identical to 230 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, to yield a sugar solution, adding to the sugar solution a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol, where the biomass composition may be optionally pretreated, or (b) contacting a biomass composition with an enzymatic composition comprising an isolated polypeptide having endoglucanase activity and comprising an amino acid sequence that is at least 90% identical to SEQ ID NO: 2, and a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol.
NOVELTY - Digesting cellulosic biomass, comprises: providing cellulosic biomass solids and slurry catalyst capable of activating molecular hydrogen in hydrothermal digestion unit; providing digestible filter aid in the unit; distributing the catalyst within the solids using fluid flow; retaining at least a portion of the catalyst in fixed location using the aid; heating the solids in the unit in the presence of the slurry catalyst, a digestion solvent, and molecular hydrogen, thus forming a liquor phase comprising soluble carbohydrates; and performing a first catalytic reduction reaction.    USE - The method is useful for digesting cellulosic biomass (claimed) and forming reaction product comprising triol, diol, and/or monohydric alcohol.    ADVANTAGE - The method: allows to retain slurry catalyst in a desired location while digesting cellulosic biomass solids; and utilizes less energy, is simple to construct and maintain, without sacrificing throughput, thus economical.    DETAILED DESCRIPTION - Digesting cellulosic biomass, comprises: providing cellulosic biomass solids and a slurry catalyst in a hydrothermal digestion unit, where the slurry catalyst is capable of activating molecular hydrogen; providing a digestible filter aid in the hydrothermal digestion unit; distributing the slurry catalyst within the cellulosic biomass solids using fluid flow; retaining at least a portion of the slurry catalyst in a fixed location using the digestible filter aid; heating the cellulosic biomass solids in the hydrothermal digestion unit in the presence of the slurry catalyst, a digestion solvent, and molecular hydrogen, thus forming a liquor phase comprising soluble carbohydrates; and performing a first catalytic reduction reaction on the soluble carbohydrates within the hydrothermal digestion unit, thus at least partially forming a reaction product comprising triol, diol, and/or monohydric alcohol in the hydrothermal digestion unit.
NOVELTY - A semi-coke is synthesized by performing low-temperature gasification using coal as raw material to produce coal gas, purifying, converting to synthetic gas, and performing decarbonization to convert synthetic gas to synthetic products.    USE - Synthesis of semi-coke (claimed).    ADVANTAGE - Process improves usage of low-temperature conversion process and sewage recycling rates, promotes development of coal projects in coal-rich areas, and has economic and environmental benefits.
NOVELTY - Biomass carbonization comprises providing carbonization furnace with heat energy heat storage circulation function to save carbon source, and carbonization barrel capable of rotating in a fixed position. The method includes stirring biomass and gradually heating, dehydrating and deacidifying, removing oil and cracking, and conveying cracking oil gas to dry distillation barrel.    USE - A biomass carbonization method.    ADVANTAGE - The method not only provides energy for carbonization process but also prevents air pollution. It is suitable for rural village or household units carbonized straw biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass carbonization device, comprising a carbide furnace (6), a guide rail (5), dry distillation barrels (8), and a movable baffle rod, where carbonization furnace body extending direction (15) and ground plane (17) form a 5-10 degrees slope (16).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the carbonization furnace and dry distillation barrel.    Guide rail (5)    Carbide furnace (6)    Distillation barrels (8)    Extending direction (15)    Slope (16)    Ground plane (17)
NOVELTY - A molded coal comprises mixture of 30-50 pts. wt. semi-coke which is obtained by low temperature pyrolysis of brown coal and 50-70 pts. wt. biomass which is forestry biomass.    USE - A molded coal (claimed).    ADVANTAGE - Process is convenient and uses broad biomass pathways. Molded coal has adjustable size.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of molded coal which involves crushing semi-coke and biomass, sieving in which particle size of biomass is less than or equal to 3 mm, putting in the mold, heating to 200-300 degrees C, shaping molded coal using hydraulic shaping device, and cooling.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of preparing molded coal. (Drawing includes non-English language text).
NOVELTY - The method involves providing an energy replacing system for providing industrial biological fuel gas for a production process, biological fuel gas purifying process and conveying process. A biomass fuel combustion process and a product output process are performed.    USE - Industrial biological gas replace petrochemical fuel gas injection molding method.    ADVANTAGE - The method enables saving energy, reducing revolution outlet, preventing pollutant discharge, improving environment, and saving industrial energy power cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an industrial biological gas replace petrochemical fuel gas injection molding method. '(Drawing includes non-English language text)'
NOVELTY - This utility model is a kind of horizontal rotary domestic garbage pyrolysis reaction kettle, by direct contact with the heated inner horizontal rotary pyrolysis reaction kettle outer and/or inner part carry out joint heating method to heat or to prevent coking to domestic garbage raw material, that is, the household garbage raw material and high-temperature inorganic heat carrier in a horizontal pyrolysis reaction kettle in domestic garbage pyrolysis reaction kettle and/or the horizontal rotation of the outer high temperature flue gas heating chamber by indirect heating, making the household garbage in a horizontal pyrolysis reaction kettle raw material cracking generated oil or/and does not contain a fuel gas with higher calorific value, the utility model belongs to the no production, high heat utilization efficiency, quick heat transmission, a no coking, no residue, household garbage continuous production of the horizontal rotary pyrolysis reaction kettle.
NOVELTY - This utility model claims a kind of combined type biomass gas decoking device, is installed on the filter body the lower end wall of the tar discharging pipe and overflow pipe connected to the tar recycling pool, a water cooling box is fixedly connected to the wall of the central hole of the circular ring baffle plate in the filter body, wherein the top end of the water cooling tank is the air baffle plate, the inner cavity with absorbing material for absorbing the air in the upper surface of the baffle plate, an oil-water separating body is the circular ring baffle plate. The water cooling tank are provided with a number on the air baffle plate, an oil-water separating body and the absorption body is more than 1; A raw fuel gas pipe is installed on the upper end of the filter wall in the top end of the filter body is provided with a sealing groove, a sealing plate is a cover in the water seal groove. A first a gas input pipe passes through the outer wall of the filter body. This kind of decoking device capable of removing most of tar in the biomass fuel gas, convenient assembly and disassembly, convenient to clean, can prolong the service life of the biomass gas furnace, has practicability and popularization value.
NOVELTY - A kind of low voltage automatic adjusting hydrogen generator, which relates to a hydrogen generator. This utility model has high temperature, large energy consumption, low efficiency, bad safety and use range is narrow; to solve the problem that the reactor for preparing hydrogen. A fuel liquid barrel and the reaction barrel set with liquid fuel, the edge of the sealing cover on the upper end face of the fuel liquid, the liquid fuel injection port is provided with a fuel liquid filling cover, a fuel liquid filling cover is processed with air hole, hydrogen air outlet pipe and the lower end of the reaction tank are connected with each other, the upper end of the gas outlet pipe is provided with a gas adjustable valve, back fire filter is provided with the upper part on the outer side wall of the fuel liquid, hydrogen air outlet pipe is connected with the side wall of the fire filter are connected with each other, the back of the upper end face of a filter is provided with an air outlet, a fuel rod is set on the upper end face of the fuel rod tray, fuel rod tray is fixed on the lower end of the inner side wall of the reaction tank through the fuel rod fixed pin. This utility model used for manufacturing hydrogen.
NOVELTY - This utility model claims a high purity normal butane production device, comprising a carbon four modified part and saturated hydrogenation, wherein the modified carbon four raw material tank and carbon four modifying reactor to obtain modified product enter into a hydrogenation reactor by cutting tower and tower and so on, and for separating a macromolecule tank and low tank and so on, finally obtaining the product n-butane by internal reaction. This provides a new high purity normal butane production device, said production apparatus of a carbon raw material, the reaction product using rate is high, and the production device is featured with simple structure, low investment, easy operation, can be recycled by the heat of the reaction product, which avoids heat energy waste, at the same time, it can realize recycling of hydrogen, circulating the regenerated air.
NOVELTY - This utility model is a kind of domestic garbage pyrolysis catalysis and gasification furnace, comprising a gasification furnace body, a furnace body top part feeding device configured in the furnace body with a drying area, area, and a bottom furnace configured to delete the furnace throat periphery configuration type of the throat area, reducing area catalyzing fixed bed, deleting a the lower part of the gas chamber, a gas chamber ash discharging machine, the utility model can make the fuel gas product for catalytic cracking of heavy oil or tar into gas component, and improves the conversion rate of the fuel gas through the gas in series through filtering to remove catalyst dust in the gas, which greatly improves the quality of the fuel gas, overcomes the problem that the production potential safety hazard overpressure block valve gas pipeline and the coke oil so as to stop and repair, to a normal production process, the utility model is provided with good industrial practicability.
NOVELTY - This utility model claims a kind of detachable biomass gasification furnace ignition device. It is provided with a step on the side wall of the gasification furnace burner port, further comprising a wind distributor, a wind distributor is provided with distributor shell, a distributor side wall of the shell is provided with an air inlet flange, distributor at the bottom of the shell is provided with a connecting flange, the connecting flange via a bolt component peripheral interface is connected with the burner, a connection flange is provided with an air cylinder, an air cylinder one end of the distributor and the inner cavity of the shell and the sealing baffle plate is matched with the sealing baffle plate is hinged on the distributor shell body on the inner wall of the other end of the air cylinder through the burner connector extends to the inner wall of the gasification furnace, distributor shell body top part is provided with a mounting flange, the mounting flange are arranged in parallel with a burner and igniter, a burner and a flame lighter passes through the air cylinder extends to the inner wall of the gasification furnace. It has simple structure, easy maintenance, good sealing performance, long service life, capable of effectively preventing gasification gas leakage, the gasification furnace operating temperature.
NOVELTY - This utility model claims a kind of using method of preparing biodiesel by catalytic cracking system, comprising a storage tank, an oil pump, a preheating tank, catalytic cracking reaction kettle and condenser, the tank body of the pre-heating tank is divided into oil storage chamber and used for heating the oil storage chamber of the heating chamber, wherein the catalytic cracking reaction kettle is provided with a heating furnace for catalytic cracking reaction kettle, the heating furnace pipe and pre-heating tank by the waste heat of the heating chamber, the heating chamber is connected with an exhaust device, the condenser is provided with exhaust outlet, said biological diesel oil storage tank, an oil pump, an oil storage chamber of the pre-heating tank, catalytic cracking reaction kettle and condenser pipe are connected in turn. This utility model not only environment-friendly, and small floor area and low cost.
NOVELTY - Clean burning biomass particle fuel boiler, and vertical parallel of the combustion furnace body and a flue gas-water heat exchanger, wherein the inner container is the upper part end cover, flame clapboard, the upper part of the furnace and the lower furnace bar is divided into gas combustion chamber, a gasification chamber and the ash chamber, the bottom is provided with a feeding pipe passes through the side wall of the outer cover and the liner is inserted into the gasification chamber from outside to inside inclined, the outlet outer side face of the ash drawer is provided with a secondary air inlet, four sides of the lower part of the side wall is opened with two air inlet, a combustion chamber inner container surrounding side walls of the lower part vent hole; the inner container upper part of the side wall of the combustion chamber is provided with a smoke gas guide tube. This utility model makes biomass particle fuel gasification fully stable, complete combustion, high temperature, improves the combustion efficiency of the fuel, at the same time, significantly reduces the dust in the gas carrying amount of the combustion air outlet flue gas cleaning, which effectively avoids the occurrence of dust and slag, improves the heat exchange efficiency of the heat exchange device, the structure is simple and compact, the operation is convenient, the operation cost is low.
NOVELTY - This utility model claims a kind of gas, heat, carbon supply biomass combustion device, a furnace body, according to the conveying direction of the first chain fire grate is divided into heating and dehydrating area, a combustion area and the extinguishing section, the further comprising a heat exchanger, a furnace body heating and dehydrating area is set on the top of the heat exchanger is connected with a steam pipe, the heat exchanger is provided with a cooling water pipe, a heat exchanger is provided with a heat storage water tank, the water outlet end of the cooling water pipe is connected with the hot water storage tank, the bottom heat exchanger is provided with a water storage tank, a water outlet of the water storage tank is connected with the spraying mechanism, the furnace combustion area an outer wall, the outer wall and the closed carbon box a flameout cell wall is provided with a water inlet and a water outlet of the water heating sleeve box, the water outlet of the water heating tank is connected with a hot water storage tank through the hot water pipe, a water heating box set the water inlet of the water inlet pipe connected with the hot water to the hot water storage tank. This utility model can make volatile component in the biomass semi-gasification burn fully and the solid carbon reserved, but at the same time a steam, hot water and charcoal.
NOVELTY - This utility model claims a biomass energy saving furnace, comprising a movable box body (1), air outlet (2), furnace end (5), the combustion chamber (7), furnace body (9), ash box (12), a blast pipe (15), a spiral feeding pipe (16), a hopper (18), wherein the combustion chamber (7) is uniformly distributed with a plurality of air inlet holes (8), a spiral feeding pipe (16) is connected with the combustion chamber (7) is connected with the bottom, the other end is provided with a hopper (18), a combustion chamber (7) is provided with a secondary wind sealing cover (11), furnace body (9) is provided with a smoke gas sealing cover (10), spiral tube (16) is provided with a blast pipe (15) is connected with the furnace body (9), gas-guide pipe (14) is connected with the spiral feeding pipe (16), the other end is extended into the air supply pipe (15). The utility model is provided with fuel gasification effect is good, high fuel utilization ratio, ignition time is short, a pipe is not easy to return to it.
NOVELTY - This utility model claims a biomass fuel half gasification furnace, comprising a shell and a hearth, wherein the hearth is a metal, in which a horizontally vertical to the hearth wall of the clapboard, the hearth is divided into upper and lower cavity, the lower cavity is a gasification chamber, the chamber is a combustion chamber, the combustion chamber is less than the diameter of the hearth, and the hearth is coaxial to the central line of the inner cylinder, and the shell is connected with the outside, the first end of which is connected with the combustion chamber of the secondary oxygen supplying pipe, the upper part of the inner cylinder is provided with a secondary oxygen hole, the lower part is connected with the reinforced secondary oxygen supply pipe network. The hearth of the metal heat transfer effect is good, so that the temperature of the secondary oxygen is greatly improved, at the same time, reinforcing the lower part of the cylinder and the inner cylinder jacket, the secondary oxygen supply uniformly into the cylinder, from the gasification chamber is a combustion gas, change the moving direction of the gas, the oxygen and the fuel gas in the gas are uniformly mixed so as to make the combustion more complete oxygen supply pipe network.
NOVELTY - The invention relates to a process for preparing a fuel of reduced corrosive effect for Diesel engines. According to the invention, the process comprises the catalytic transesterification of sunflower oil triglycerides in the presence of methanol, wherefrom there results, as a main product, a biodiesel fuel component which is additivated with 0.1% by weight tert-butyl amine, finally resulting in a fuel to be used as such or in admixture with gas oil, having a corrosion rate of a submerged stainless steel electrode of 0.207 E-3 mm/year and physical and chemical properties in accordance with the standard EN 14214.
NOVELTY - A kind of cotton stalk section of robot, belonging to the technical field of biomass fuel. The cotton stalk section of a whole is funnel structure, the upper part of the feeding port is opened, the feed box is provided with multiple shifting roller, the roller on one side of shifting roller motor, a shifting roller is provided with shifting gears, the feed box is set at the lower part of section, section box is provided with a movable cutter roller and a fan, a movable cutter roller through the transmission belt is connected with the movable cutter motor, the movable knife roll is provided with multiple irregular movable knife rest and the movable knife frame is provided with movable knife, section two sides of upper part of the water tank is provided with a discharging port, a main body of the first side is provided with a control panel. This utility model replaces the manual feeding, it only needs one person using shovel car, feeding to the material feeding port, saves the labour, improves the working efficiency, it is not easy to be blocked, convenient to feed and discharge, save work time, reduces the labour intensity, improves the working environment, it is good for the health of the operator.
NOVELTY - A kind of biomass gas extracting vaporizer, comprising a vaporizing tank, a gasification tank is provided with a gas outlet, a water outlet and the air inlet of gasification tank is provided with a carbonization material sealed double layer device, the bottom of gasification tank is provided with a discharging port, the lower part is provided with a discharging port carbonization hopper, the feeding pipe and the horizontal piston cylinder sleeve sealing of the tank, the horizontal piston cylinder sleeve and the upper part of the feeding hopper is connected with the piston type indirect closer in the horizontal piston cylinder sleeve for sealing, a piston type indirect closer to a curved rod, curved rod installed on the electric speed reducer. And the tank gasification from biomass fuel, capable of separating extracting a large amount of natural gas, and then increased by about 50% by the heat productivity, biomass, discharge capacity of the boiler is reduced by 80%, no harmful gas and methane discharge, the device can continuously lift, energy-saving and environment-friendly.
NOVELTY - An electrolyte material has electronically insulating oxide of base metal and greater than or equal to 1 additional metal (oxide) which enhances the base metal with ionic conductivity, where the electrolyte material has a layer structure with B-layers consisting of 30-90% metal atoms and/or ions of base metal and A-layers consisting of 30-90% metal atoms and/or ions of additional metal.    USE - Electrolyte material for producing fuel cells (claimed).    ADVANTAGE - The electrolyte material has improved ionic conductivity at lower temperatures.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing electrolyte for fuel cell.
NOVELTY - Preparing entecavir, comprises deprotecting (9R)-9-((3R)-3-methyl-2-methylene-cyclopentyl)purine derivatives (III) in a solvent in the presence of Lewis acid.    USE - The method is useful for preparing entecavir, which is useful for preparing hydrate of entecavir (all claimed).    ADVANTAGE - The method simply and rapidly provides entecavir with reduced reaction steps and solvent consumption, and high yield (more than 80%) and chemical purity (more than 98%) in an environment friendly manner.    DETAILED DESCRIPTION - Preparing entecavir, comprises deprotecting (9R)-9-((3R)-3-methyl-2-methylene-cyclopentyl)purine derivatives of formula (III) in a solvent in the presence of Lewis acid.    R1-R3 = hydroxyl protecting group, preferably acetyl, beta -methoxyethoxymethyl ether, bis-(4-methoxyphenyl)phenylmethyl, methoxymethyl ether, (4-methoxyphenyl)diphenylmethyl, p-methoxybenzyl ether, tetrahydropyranyl, triphenylmethyl, benzyl, benzoyl or silyl ether protecting group; and    R4 = amino protecting group, preferably triphenylmethyl, (4-methoxyphenyl)diphenylmethyl, tert-butyloxycarbonyl, benzyloxycarbonyl, 2-biphenyl-2-propoxy carbonyl, formyl or trifluoroacetyl.    An INDEPENDENT CLAIM is included for preparing a hydrate of entecavir, comprising adding the entecavir to an aqueous solvent to form a solution, warming the solution to a temperature of 80-100 degrees C, and cooling the solution gradiently in more than 2 steps of decreasing the temperature of the solution by 5-20 degrees C in 0.5-2 hours.
NOVELTY - Converting biomass into liquid fuels involves (a) subjecting a starting material comprising biomass to pyrolysis under pyrolysis conditions to give pyrolysis oil, (b) subjecting pyrolysis oil to non-catalytic high temperature high pressure (HTHP) treatment comprising at least two steps and separating an aqueous phase and HTHP treated pyrolysis oil, and (c) subjecting HTHP treated pyrolysis oil to hydroprocessing in the presence of at least one hydroprocessing catalyst and hydrogen, where an effluent comprising one or more hydrocarbons boiling in the liquid fuel hydrocarbon is obtained.    USE - The method is useful for converting biomass into liquid fuels including hydrocarbon fractions, gasoline, kerosene, jet fuel, diesel oil, naphtha, blending components for transportation fuels, heating oil, solvents, fine chemicals and building-block chemicals (all claimed), where the liquid fuel is useful in boilers, gas turbines and diesel engines.    ADVANTAGE - The method is capable of economically converting biomass into liquid fuels with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a product obtainable by the above method.
NOVELTY - A fluidized bed combustor consists of a combustion chamber (11) adopted to contain a fluidized bed (12) of particulate material, a gas-permeable support on which the bed is supported within the component, an air inlet through which air is blown into the bed, an exhaust outlet provided at one end of the component, and an electric heating coil (13).    USE - Fluidized bed combustor is used for burning biomass, low-quality coal, and waste materials.    ADVANTAGE - The fluidized bed combustor reduces air pollution by controlling gas emission (emission of sulfur dioxide) from solid fuel combustion using a laboratory scale fluidized bed combustor with a cross-section area of approximately 0.0123 m2. The combustor is suitable for domestic application, simple, clean, modular, and user-friendly, reduces cost, increases productivity, and requires less maintenance operations. Heat from solid fuel combustion maintains the bed temperature while temperature of the entire bed is stabilized by heat transfer. The bed particles are prevented from crushing or melting due to the low combustion temperature at 850 degrees C. The transfer of heat does not only occur through radiation, but also through direct conduction from the bed molecules to the surface of heat exchanger.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a bench-scale fluidized bed combustor.    Combustion chamber (11)    Fluidized bed (12)    Electric heating coil (13)
NOVELTY - Processing (M1) a biomass involves separating a solid saccharified biomass from a liquid medium, and saccharifying the solid saccharified biomass.    USE - For processing a biomass; and for saccharification of biomass. The biomass is cellulosic or lignocellulosic biomass; and is selected from paper, paper products, paper waste, wood, particle board, sawdust, agricultural waste, sewage, silage, grasses, straw, wheat straw, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, corn stover, alfalfa, hay, coconut hair, seaweed, and/or algae (claimed).    ADVANTAGE - The method increases saccharification effectiveness; is more cost effective and flexible; has less process variability (e.g. less viscosity variability, temperature variability and/or pH variability); and allows high throughput.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for saccharification (M2) of biomass involving saccharifying a solid biomass in a liquid; separating solid saccharified biomass from the liquid; removing the liquids from the separated saccharified biomass, and adding liquid and a saccharifiying agent to separated saccharified biomass.
NOVELTY - The system (10) has fuel cell stacks (30) to maintain fluid communication with water reservoir (20), and provided with cathodes and anodes. A proton exchange membrane is used for separating water in reservoir into hydrogen and oxygen, when current is applied across cathodes and anodes. Each fuel cell stack has gasket, and through hole for passage of hydrogen or oxygen through gasket. The channels are formed in gasket, and are sized and shaped to allow passage of hydrogen or oxygen to or from through hole and gasket edge portion.    USE - Hydrogen fuel system for internal combustion engine mounted in motor vehicle such as semi tractor trailer, car and truck.    ADVANTAGE - The oxygen and the hydrogen are separated from one another, and pure hydrogen is less combustible or explosive without presence of oxygen, so that the hydrogen fuel system is configured to minimize the risk of inadvertent combustion or explosion of the hydrogen. The performance of the internal combustion engine is improved by using the hydrogen fuel system. The fuel cells provided in the hydrogen fuel system can produce more hydrogen for engines with larger displacement. The fuel cell stack can be electrically coupled to the electrical power source of the internal combustion engine, and hydrogen fuel system does not require the additional electrical power source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen fuel system in the closed configuration.    Hydrogen fuel system (10)    Housing (12)    Water reservoir (20)    Fuel cell stack (30)    In-vehicle display (110)
NOVELTY - A solution of linezolid is provided in water at 80-95 degrees C, and the solution is stirred at 80-95 degrees C. The solution is cooled and crystallized slowly at a temperature of less than 35 degrees C. The solution is cooled slowly at temperature of less than 35 degrees C, crystallized to obtain reaction mass. The highly pure crystalline form III-linezolid is recovered from the reaction mass.    USE - Preparation of crystalline linezolid (claimed).    ADVANTAGE - The method economically, efficiently and environmentally-friendly provides crystalline linezolid with high yield and high purity.
NOVELTY - The apparatus comprises a de-watering chamber for drying a sludge supplied from a sludge supply pipe, an oil supply pipe in which oil is supplied to moisturize the sludge along the inner portion of the de-watering chamber, a waste heat supply tube supplying heat to an inner tube of a boiler, where an inner portion of the de-watering chamber is maintained in vacuum condition, and the generated heat from the waste heat supply tube is used to stabilize the processing of lime sludge in the de-watering chamber.    USE - The apparatus is useful for recycling sludge into fuel (claimed) and a fertilizer from foul water processing facilities.    ADVANTAGE - The apparatus can process the sludge by vacuum suction, oil substitution, and the waste heat process so as to minimize the sludge drying time and can economically and effectively generate fuel with increased calorific value.    DETAILED DESCRIPTION - The apparatus comprises a de-watering chamber for drying a sludge supplied from a sludge supply pipe, an oil supply pipe in which oil is supplied to moisturize the sludge along the inner portion of the de-watering chamber, a waste heat supply tube supplying heat to an inner tube of a boiler, where an inner portion of the de-watering chamber is maintained in vacuum condition, and the generated heat from the waste heat supply tube is used to stabilize the processing of lime sludge in the de-watering chamber. An oil extractor is used for extracting oil from the sludge, where the extracted oil is resupplied again to the de-watering chamber through the oil supply pipe.
NOVELTY - A diesel oil contains 50-80 pts. wt. animal fat, 30-45 pts. wt. vegetable oil, 9-10 pts. wt. diesel oil, 5-9 pts. wt. kerosene, 15-20 pts. wt. ethanol, 8-16 pts. wt. cleaning agent, 5-8 pts. wt. emulsifier, 9-15 pts. wt. antioxidant, and 14-23 pts. wt. water.    USE - A diesel oil (claimed).    ADVANTAGE - Diesel oil is efficient, clean, environment-friendly, and low in cost, and has high stability and wide raw material source.
NOVELTY - A coal slurry and biomass composite comprises 100 pts. wt. slurry and 10-500 pts. wt. biomass on dry basis with biomass particle size of less than or equal to 20 mm in which composite coal is pressed in briquette molding machine to obtain shape and mechanical strength.    USE - A coal slurry and biomass composite (claimed).    ADVANTAGE - The coal composite reduces amount of non-renewable energy and has microporous structure and good combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of coal slurry and biomass composite briquette which involves uniformly mixing 100 pts. wt coal slurry and 10-500 pts. wt. biomass on dry basis with biomass particle size of less than or equal to 20 mm, and pressing mixed briquette in molding machine to obtain shape and mechanical strength.
NOVELTY - A microalgae biofuel is prepared by mixing microalgae with alcohol-water solution in reactor, heating reaction at 260-360 degrees C and pressure of 7-22 MPa for 15-45 minutes in which mass-to-volume (g:ml) ratio microalgae:alcohol-water solution is 1:5-20 and alcohol-water solution contains 20-80 vol.% alcohol, adding organic solvent to extract reaction liquid containing organic solvent phase, alcohol-water phase, and solid residue, settling, suction filtering to separate solid residue, and distilling organic solvent under reduced pressure at 20-40 degrees C with gauge pressure of 0.085-0.095 MPa.    USE - Preparation microalgae biofuel (claimed).    ADVANTAGE - The preparation process is simple, low cost, and environment-friendly, has low moisture content, low ash content, and low acid value, and improves biofuel yield and quality.
NOVELTY - Preparing dehydroandrographolide succinate comprises adding andrographolide and succinic anhydride with anhydrous sodium sulfite as antioxidant under the protection of nitrogen, heating the mixture, stopping the reaction by cooling and then adding non-polar solvent such as weak acid monohydrate, concentrating and decoloring the mixture, dropping in alkaline solution, reacting the mixture to obtain clear solution, adding acetone into the water for crystallizing and then filtering the under the protection of nitrogen to obtain filter cake and drying in vacuum.    USE - The method is useful for preparing dehydroandrographolide succinate (claimed).    ADVANTAGE - The method simply and economically prepares the dehydroandrographolide succinate in an environmentally-friendly manner with high purity.    DETAILED DESCRIPTION - Preparing dehydroandrographolide succinate comprises adding andrographolide and succinic anhydride with anhydrous sodium sulfite as antioxidant under the protection of nitrogen, heating the mixture at 10-30 degrees C to react at 45-95 degrees C for 4-20 hours, stopping the reaction by cooling and then adding non-polar solvent such as weak acid monohydrate, concentrating and decoloring the mixture, adding acetone in water under the protection of nitrogen to reduce at -10 degrees C to 5 degrees C, dropping in alkaline solution, reacting the mixture to obtain clear solution, adding acetone into the water for crystallizing and then filtering the under the protection of nitrogen to obtain filter cake and drying in vacuum.
NOVELTY - The reactor has a waste gas collecting pipe provided with multiple exhaust gas inlets. A flameproof block is provided with a flame proof component. A gas injection unit is mounted on a top part of a vortex plasma reactor main body. Another gas injection unit is mounted on the vortex plasma reactor main body, a draft tube reactor body, a plasma torch body, and a high frequency induction coil. The waste gas collecting pipe collects plasma waste gas. The vortex plasma reactor main body is connected to a reactor flow guide pipe by the latter gas injection unit and filled with the plasma waste gas.    USE - Vortex plasma reactor for PFCs waste gas treatment.    ADVANTAGE - The reactor completely prevents damage of the high frequency induction coil at certain reaction time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a vortex plasma reactor.
NOVELTY - Production of high-quality coal involves processing biological oil or straight-run kerosene fraction of secondary feedstock as raw material oil, hydrothermally-treating primary feedstock through at least two hydrogenation reaction zones of reactor filled with hydrogenation catalyst comprising tungsten, molybdenum, nickel and cobalt, separating bio-oil and hydrogen, separating primary hydrogenation reaction zone effluent into gas phase and liquid phase, recycling gas phase, separating liquid and secondary raw oil obtained under hydrogenation conditions in secondary reaction zone.    USE - Production of high-quality coal (claimed).    ADVANTAGE - The method efficiently and economically provides high-quality coal having high storage stability.    DETAILED DESCRIPTION - Production of high-quality coal involves processing biological oil or straight-run kerosene fraction of secondary feedstock as raw material oil, hydrothermally-treating primary feedstock through at least two hydrogenation reaction zones of reactor filled with hydrogenation catalyst comprising tungsten, molybdenum, nickel and cobalt, separating bio-oil and hydrogen, separating primary hydrogenation reaction zone effluent into gas phase and liquid phase, recycling gas phase, separating liquid and secondary raw oil obtained under hydrogenation conditions in secondary reaction zone, processing product in tertiary reaction zone, separating tertiary reaction zone effluent by distillation and obtaining naphtha, high-quality kerosene oil fraction and tail.
NOVELTY - Preparation of biological diesel oil, involves: (1) under a near-critical or supercritical reaction condition, contacting grease raw material and monohydric alcohol to obtain crude fatty acid ester mixture; (2) removing water from crude fatty acid ester mixture obtained in the step (1) to make the water content in the mixture of not greater than 1 wt.%; and (3) under near critical or supercritical reaction condition, contacting water removed crude fatty acid ester mixture obtained in the step (2) with monohydric alcohol.    USE - For preparation of biological diesel oil (claimed).    ADVANTAGE - The method for preparation of biological diesel oil obtains acid number value of qualified biodiesel product under a mild reaction condition; provides stable deacidification effect; and can give consideration to the yield of the bio-diesel.
NOVELTY - The method involves placing carbon raw material into a furnace, and increasing temperature of a heating resistor for a generator. The carbon raw material is rice hull, rice, peanut shell, cotton shell, corn cob, saw dust, wood chips, wood shavings, bamboo, grain shell, and/or coconut shell.    USE - Sealed continuous high purity water coal production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating a sealed continuous high purity water coal production method.
NOVELTY - The utility model claims a scrap as the raw material for preparing fuel, comprising a garbage breaking crush machine, sorting machine and dewatering machine, the sewage purification treatment device, a flue gas waste heat boiler and smoke purifying device for preparing fuel injection molding device, wherein, for preparing fuel to a main separating tank, a tank and a gas storage cabinet are connected in turn according to the pyrolysis reactor, a condenser, a gas-liquid, and the fast mechanical sorting and domestic garbage, overcomes the ecological residential area for classifying garbage, the carbohydrate solid waste first crushed and dehydrated garbage can effectively reduce volume and improve the garbage thermal value, the utility model domestic waste produced does not contain a high heating value fuel gas or fuel oil, so as to carry out large scale, the energy of the treating device for automatically sorting household waste, reducing and harmless.
NOVELTY - The utility model claims a heat supply device, that is a kind of dynamic biomass gasification furnace, wherein the furnace body (1), (2) is provided with a heat storage chamber (3), heat storage chamber (3) is provided with a plurality of heat absorption block (4), a heat storage chamber (3) is provided with a fuel gas pipe (5). Blast pipe (8) passes through the heat storage chamber (3) enters the hearth (2), a hearth (2) and the inner wall is a curved surface, the hearth is connected with a plurality of circular arc surface is smooth so as to become a (2) and the inner wall is connected with heat storage chamber (3) and a hearth (2) of the heat transmission port (10), a hearth (2), a blast pipe (8) is provided with positive (11) and negative (11) one side of the pressure plate (16). Furnace body (1) outside the blast pipe (8) is connected above the fuel conveying pipe (6). The air inlet of the fan (7) are respectively connected with the air inlet pipe (14) and smoking pipe (9), the air inlet pipe (14) and smoking pipe (9) is provided with a switch (15). The beneficial effects are as follows: storage of heat energy, fuel and combustion-supporting air pre-heating to obtain a . Flue gas in hearth a hearth keep stable the cracking condition through fan cycling. Fuel enters the hearth with air under the dynamic state of the upper and lower rotary cracking, cracking. A burnout of fuel sucked by blast pipe, spraying cracking, gasification more fully.
NOVELTY - This utility model claims a suction type. pyrolyzing gasification furnace, comprising an upper end with a furnace cover and a gasification furnace fuel gas outlet, the upper part of the gasification furnace body is further provided with air distribution device, an ignition device, a dust removing device and a temperature monitoring device, wherein the gasification furnace body is provided with a double-taper furnace liner, and the bi-conical furnace from top to bottom in turn to form drying space, space, space and reducing space. This utility model is furnace adopts a double-tapered structure is helpful for form a whole direct current in the furnace, which effectively reduces the bridge and arch tendency, improve the gas yield. The furnace body and the ignition system, an air distribution system, a dust removing system and a temperature monitoring system combined with together to form automatic household garbage treating system.
NOVELTY - A kind of energy-saving firewood stove, comprising a stove main body, further comprising a base (6), a furnace door (7), the internal heat insulation layer (8) and an annular fire are matched with plate (9). This utility model has advantages of fire adjusting process is simple, the effect is good, the burn quickly and partial high temperature, to form the best of the wood and dry environment, the wood firewood gasification effect, the flame temperature is high, which reaches the purpose of energy saving and emission reduction, the cooker receiving the flame temperature is more uniform, using effect is better.
NOVELTY - Separating renewable materials from microorganisms, comprises: conditioning cell walls of microorganisms containing a renewable material to form, open or enlarge pores; and removing at least a portion of renewable material through the pores.    USE - The process is useful for separating renewable materials from microorganisms, preferably oleaginous yeast belonging to the genus Rhodotorula, Pseudozyma, or Sporidio bolus, where the renewable materials are useful to produce biofuels (all claimed), a food product, a pharmaceutical composition, a cosmetic product, and/or an industrial composition.    ADVANTAGE - The method provides the renewable material with high yield and without maximal disruption of the cell wall structures in a cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) delipidated microorganisms made by the process;    (2) a process for extraction of lipids from oleaginous yeasts, comprising conditioning oleaginous yeast by a thermal treatment to increase cell wall porosity and removing lipids from the oleaginous yeast with cell walls substantially intact;    (3) delipidated yeast with cell walls substantially intact and with mesopores; and    (4) a process for production of biofuels, comprising culturing yeast on sugar to accumulate lipids within cell walls of the yeast, conditioning the yeast to form or enlarge pores in the cell walls, removing the lipids through the pores in the cell walls, separating the lipids from the yeast and converting the lipids into a biofuel.
NOVELTY - The apparatus has a reaction chamber positioned relative to a microwave radiation generator to receive microwave generation radiation from the microwave generation generator. A temperature probe detects a temperature within the reaction chamber. A controller receives the temperature within the reaction chamber from the temperature probe. The controller controls production of microwave radiation by the microwave radiation generator to maintain the temperature of the reaction chamber at the predetermined temperature until a reaction in the reaction chamber is completed.    USE - Apparatus for rapid synthesis of catalyst of fuel cell mounted in vehicle.    ADVANTAGE - The ultra-fine metal catalyst nano-particles can be produced with the low degree of agglomeration, and the dispersion on the catalyst support can be improved, thus the catalytic activity can be optimized.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process for rapid synthesis of catalyst.    Step for preparing solution comprising solvent, precious metal precursor, catalyst substrate, reducing agent and stabilizer (10)    Step for increasing temperature of solution with microwave irradiation at controlled rate to predetermined temperature (16)    Step for holding solution at predetermined temperature until reduction and deposition are completed with microwave irradiation (18)    Step for cooling solution (20)    Step for washing catalyst particles (22)
NOVELTY - The method involves sintering the transmitted sheets. The transmitted sheets of two fields are conjugated to form the air electrode in the electrolyte phase. The conjugated transmitted sheet is provided on fuel anode sheet. The electrolyte (130) and fuel anode (140) are formed.    USE - Method for manufacturing solid oxide fuel cell.    ADVANTAGE - The manufacture yield of the solid oxide fuel cell can be improved at low cost while reducing the wastage.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating the manufacturing process of solid oxide fuel cell.    Defection portion (10)    Solid oxide fuel cell (100)    Electrolyte (130)    Fuel anode (140)
NOVELTY - A material (22) is exposed to hydrogen. The hydrogen-exposed material is irradiated. The characteristic of the material is determined based on the result of the irradiation in order to analyze the material.    USE - Method of analyzing material is used for forming catalyst used in fuel cells for generating electricity.    ADVANTAGE - The analyzed material is economically provided to facilitate electrochemical reaction in fuel cell, and exhibits X-ray diffraction patterns.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus (20).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus.    Apparatus (20)    Material (22)    Chamber (24)    Source (26)    Output device (28)
NOVELTY - The system has a condenser (20) which condenses vapor which is passed to an evaporator (30). A cooling function is performed by evaporation of heat using a refrigerant in the evaporator. The refrigerant is absorbed between an absorber (40) and a low temperature regenerator (10). A fuel cell main structure is provided to eject an exhaust gas with a power generation with an electrochemical reaction. An absorption system is driven to a lithium bromide refrigerant. Waste heat of a fuel cell generation system is refluxed to fuel cell main structure and heat recovery system.    USE - Heating and cooling system installed in building, using waste heat of fuel cell generation system.    ADVANTAGE - The cooling efficiency of the fuel cell can be improved. The heat generation efficiency of the fuel cell can be improved. The durability of the fuel cell can be extended. The fuel required for the fuel cell generation system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of the heating and cooling system. (Drawing includes non-English language text)    Low temperature regenerator (10)    High temperature regenerator (12)    Condenser (20)    Evaporator (30)    Absorber (40)
NOVELTY - A biodiesel oil is prepared by mixing oil or fatty acid and methanol to obtain methyl ester crude product, and distilling.    USE - Non-catalytic manufacturing method of biodiesel oil (claimed).    ADVANTAGE - Manufacturing method is simple and environment-friendly, has high conversion rate, and reduces equipment corrosion, and product has high purity, and light color without peculiar smell.
NOVELTY - Anti-slagging combustion method of biomass-sludge comprises adding flocculating agent to secondary sedimentation tank sludge at flocculating agent to dry sludge weight ratio of 1:(200-500), flocculating and concentrating, adding calcium oxide modifier at calcium oxide modifier to dry sludge weight ratio of 1:(10-100), dehydrating, drying, crushing, mixing with biomass and performing combustion.    USE - Anti-slagging combustion method of biomass-sludge used for preparing shaped fuel (claimed).    ADVANTAGE - The method avoids direct adding of magnesium oxide, aluminum hydroxide, calcium oxide and other combustion additives, thus saving resource and avoiding secondary pollution.
NOVELTY - A plasma garbage biomass gasification device, claims a plasma gasifying furnace device comprises a plasma gasification furnace and spiral feeder, mainly composed of a furnace body, a cathode, an anode, a furnace body and a top cover, wherein the lower part of the lower furnace body with a cavity, a cathode is provided with a lower furnace body, the upper part of the inner cavity of the cavity of the lower furnace body of the cathode is connected with the outer edge of the cathode end of the cylinder upper end is bell mouth shape, a loudspeaker with a rotational flow groove, the furnace body is connected to the upper end of the lower furnace body, the anode is set on the upper part in the furnace body, the axial center of the anode with a through hole, an axial center through hole compression hole, rotating body structure wall body of the anode with a cooling water sleeve, the end of the pole part is V shaped, the lower anode part of the V-shaped surface extends into the bell mouth of the upper end of the cathode and has a gap, a top cover is set on the upper end face of the anode and the upper part of the furnace body, with a synthetic gas output interface is set on the top cover. This utility model is the domestic garbage or biomass is converted into hydrogen-rich high quality synthesis gas, and removing dioxin pollution problem.
NOVELTY - A kind of garbage cracking furnace, the character is that: a speed reducer is set on the lower part of the furnace body, the inside of the speed reducer is provided with a speed reducer motor, a speed reducer and a transmission shaft, the transmission shaft passes through the shaft hole of the speed reducer extends into the top of the furnace body, a speed reducer and a transmission shaft which is connected with a coupler, discharging pipe is inclined into a speed reducer, the bottom of the furnace body is provided with slag discharging port is connected with the discharging pipe, uniformly provided with a shaft coupling and a fire grate are provided with cycloid electric motor, a fire grate with the cycloid motor; the top of the furnace body is provided with an explosion. It can reach the following beneficial effects: large-capacity pre-positioned cost and maintenance cost is low, the operation is simple, high safety performance, the Chinese is easy to popularize, sufficient combustion, combustion control, by two of fission, the smoke dust; high device utilization rate, low ash, low harmful gas discharge.
NOVELTY - A sulfur tolerant catalyst comprises 2-40 wt.% main metal active component, 0.5-35 wt.% auxiliary agent, and 50-97.5 wt.% carrier.    USE - Sulfur tolerant catalyst used for slurry bed methanation (claimed).    ADVANTAGE - The catalyst has higher catalytic activity and selectivity, and long service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst comprising calcining carrier at 400-600 degrees C for 1-8 hours; mixing active component soluble salt and auxiliary agent soluble into a mixed solution, stirring at 15-60 degrees C and 30-300 revolutions/minute, adding calcined carrier in mixed solution, stirring for 2-36 hours, standing for 1-12 hours, and evaporating solvent in water bath at 50-90 degrees C; drying impregnated product at 70-150 degrees C for 4-36 hours, grinding to 40-200 mesh, baking at 350-600 degrees C for 1-8 hours to obtain precursor; introducing 5-25% hydrogen and 75-95% mixed nitrogen atmosphere to precursor at a flow rate of 50-200 ml/minute, controlling two-section program temperature, increasing temperature at a speed of 0.5-10 degrees C from the room temperature to 350 degrees C, performing constant temperature reduction and raising temperature to 450-700 degrees C at a speed of 0.5-5 degrees C for 1-12 hours; and cooling material to room temperature in a nitrogen atmosphere.
NOVELTY - A biological composition comprises 1-8 wt.% triazine, 50-70 wt.% Kathon (RTM: microbiocide), and balance water.    USE - Biological composition used as industrial bactericide for metal working fluid, paint, adhesive, paper and biodiesel oil (claimed).    ADVANTAGE - The environment-friendly composition has fast antibacterial function rate, lasting anti-corrosion property and broad sterilization spectrum.
NOVELTY - This utility model claims an electrolytic cell, is provided with an electrode section in the electrolytic cell, the electrode area of the vertical is provided with a non-electrolytic cell. After the utility model adopts said solution, the electrolytic cell when working, the electrolyte can flow along the cross section in the vertical direction, wherein the upper part of the electrolysis zone capable of temporarily collecting a part of hydrogen can reduce the hydrogen bubble content in the electrolyte solution phase, which reduces the ohm voltage drop of the solution.
NOVELTY - This utility model claims a kind of a removing container, comprising a tank body, is provided with an electrolyte inlet on the side wall of the tank body is provided with an electrolyte outlet at the bottom of the tank body, besides, it is provided with an automatic exhaust device on the upper part of the tank body. When the electrolyte and hydrogen mixture enter into the tank body and the liquid is discharged from the bottom of the liquid outlet, the gas in the upper part of the gas to a certain height on the top of the floating ball gravity falling edge, an exhaust valve body is reduced, at this time, a gas discharged from the top of the gas and liquid is discharged for floating ball supporting the valve body closed at the moment the first exhaust work is finished, the exhaust process depending on buoyancy principle; Therefore, it can effectively release the hydrogen in the electrolysis bath, reduce the influence of gassing effect.
NOVELTY - This utility model claims a sludge by using waste oil residue for producing gasoline straw heating furnace, relating to the technical field of heating furnace. A first square of the heating furnace body (2), a heating furnace body is equipped with an electric heater (3), a heating furnace body is equipped with a controller (1), a feeding port (4) the heating furnace body, a heating furnace body side part is provided with a discharging port (5), a discharge hole is equipped with a valve, a temperature sensor (7) and a pressure sensor (9) the heating furnace body, a heating furnace body upper part of the inner side is provided with a liquid level sensor (8), a temperature sensor, a pressure sensor, a liquid level sensor and a heater are respectively connected with the controller. In the utility model solves the problem that the waste oil sludge oil residue straw for producing gasoline production, heating the mixed raw material, the heating furnace temperature is difficult to control and the safety performance is poor.
NOVELTY - The device has an annular sieve plate (14) formed with an annular groove structure air duct (18) for discharging slag. A slag inlet is arranged opposite to the air duct along tangential direction. The annular sieve plate is uniformly formed with large sieve pores (15) and a small sieve pore (16). The annular sieve plate is connected with a vibrator (11). An air inlet (8) is provided with a slag discharging air intake valve (9). A slag-drip opening (4) is formed in a slag discharging valve (3). A lower air duct (19) is formed in a combustion air inlet (7).    USE - Biomass gasification furnace slag discharging device.    ADVANTAGE - The device utilizes vibration of a vibrating screen to achieve discharging of ash and the slag into the duct through the large and small sieve pores. The device has convenient slag discharging, and eliminates complex discharging mechanism problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification furnace slag discharging device.    Slag discharging valve (3)    Slag-drip opening (4)    Combustion air inlet (7)    Air inlet (8)    Slag discharging air intake valve (9)    Vibrator (11)    Annular sieve plate (14)    Large sieve pores (15)    Small sieve pores (16)    Annular air duct (18)    Lower air duct (19)
NOVELTY - The utility model claims hydrogen-preparing device, especially relates to a kind of a sodium borohydride hydrogen production device. A kind of a sodium borohydride hydrogen production device, comprising a cathode electrode and an anode electrode and filled with sodium borohydride solution of the electrolytic cell, the cathode electrode and the anode electrode is connected with a direct current power supply. This utility model using sodium borohydride aqueous solution and direct current voltage electrode, the charge transfer the electrolyte interface acceleration, the electrode catalytic activity, a electrode electro-catalysis function, promoting sodium borohydride decomposition reaction, preparing hydrogen by electro-catalysis and electrolysis hydrogen by the maximum difference is that the electro-catalysis by a far smaller than a decomposition energy so as to save the energy consumption, producing the beginning and ending of the hydrogen and hydrogen production can be through adjusting the current and voltage between electrodes, a control is greatly improved.
NOVELTY - This utility model claims a kind of double-cyclic anaerobic reactor, comprising a tank body, a tank body from bottom to top in turn is provided with a water distribution system, a sludge reaction bed, the first level three phase separator, a sludge reaction bed, a level three phase separator, the first level three phase separator is provided with a connected with the first gas-liquid separator is a gas collecting pipe, the second level three phase separator is provided with a connected with the first gas-liquid separator is a gas collecting pipe, the first side wall is provided with a gas-liquid separator, circulating reflux pipe is connected with the water distribution system is provided with a biogas outlet pipe, the side wall of the tank body in the secondary sludge reaction with the gas-liquid separator is connected with the second pipeline, the second gas-liquid separator is connected with the water distribution system is a circulating reflux pipe, the side wall of the water outlet pipe. The utility model has low energy consumption, high production efficiency is high, the reliability is good, it is suitable for industrial mass production.