NOVELTY - The die has a heat rod that is contained in a heat rod accommodating chamber of main portion. A seating surface is arranged in upper end of main portion and is provided with a primary connecting rod bruise. A fixture is arranged for covering the upper portion of the heat rod and is provided for securely fixing the heat rod in the heat rod accommodating chamber.    USE - Molding die of waste molder.    ADVANTAGE - The damage of the heat rod is prevented. The replacement and repair work of the heat rod can be performed conveniently.
NOVELTY - A low valuable lake fish species disposing method involves collecting dead low valuable lake fish species, and composting the dead fish by 20-30% organic material. Constant humidity of compost mass is maintained at 60-70% of ambient temperature, and the compost mass is sprinkled with 0.5-1.5% brown coal, where the organic material is straw, sawdust or bark.    USE - Method for disposing a low valuable lake fish species.
NOVELTY - Producing a biomass comprising inoculating a microalgae in a culture medium, and adjusting pH of the medium to be 9, where the culture medium is prepared by adding sodium nitrate, potassium nitrate, platinum pentoxide, monopotassium phosphate, magnesium sulfate, magnesium nitrate hexa hydrate, calcium nitrate, potassium sulfate, EDTA disodium salt solution, ferric chloride hexa hydrate, cobalt nitrate hexa hydrate, manganese sulfate penta hydrate, zinc sulfate octa hydrate, copper sulfate penta hydrate, alloy of ammonia molybdenum and oxygen compound ((NH4)6MO2O24) and nitric acid.    USE - The method is useful for producing a biomass i.e. pyrolysate (all claimed).    ADVANTAGE - The method is capable of highly producing the biomass using the microalgae.    DETAILED DESCRIPTION - Producing a biomass comprising inoculating a microalgae in a culture medium, and adjusting pH of the culture medium to be 9, where the culture medium is prepared by adding (in mg/l): sodium nitrate (200-240); potassium nitrate (200-240); platinum pentoxide (130-200); monopotassium phosphate (50-100); magnesium sulfate (20-45); magnesium nitrate hexa hydrate (25-45); calcium nitrate (50-100); potassium sulfate (25-45); EDTA disodium salt solution (20-45); ferric chloride hexa hydrate (0.5-1.5); cobalt nitrate hexa hydrate (0.01-1.0); manganese sulfate penta hydrate (0.01-1.0); zinc sulfate octa hydrate (0.01-1.0); copper sulfate penta hydrate (0.001-0.1); alloy of ammonia molybdenum and oxygen compound ((NH4)6MO2O24) (0.001-0.1); and nitric acid (0.01-1).
NOVELTY - The system has liquid JET apparatus (200) and underwater motor (800) that are installed at upper layer of gas generation conduction tub at specific interval. A non-woven fabric (102) is installed in upper side of through-hole through garbage mixture cabinet. The garbage mixture cabinet is provided with the gas collector (900) that is closed at upper end portion of conduction tub. The garbage mixture cabinet is provided with garbage mixture hanger. A collecting gas outlet is connected in one side of the gas collector for discharging the collecting gas to outside.    USE - Refuse disposing system for disposing garbage of domestic waste, sludge, human excrement and food waste.    ADVANTAGE - The garbage of domestic waste, sludge, human excrement and food waste can be disposed and can be recycled effectively, so that the environmental contamination can be minimized. Hence the production cost can be minimized. The fuel efficiency of the system can be improved. The fossil fuel can be gradually exhausted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing gas using refuse disposing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the process bath.    Non-woven fabric (102)    Liquid JET apparatus (200)    Underwater motor (800)    Gas collector (900)    Process bath (1000)
NOVELTY - Method for processing food waste using waste culture soil, involves (a) drying food waste containing 90% or more moisture content until moisture content in the food waste is 40-50%, (b) mixing waste culture soil, rice bran, molasses and humidity adjusting agent with the dried food waste, controlling the moisture content of the mixture at 60-70%, and generating a reaction, and (c) fermenting the resultant product of the reaction for 3-4 days.    USE - The method is useful for processing food waste (claimed).    ADVANTAGE - The method suppresses the bad smell generated while disposal of food, is cost-effective, and consumes less time.
NOVELTY - An organic waste degradation method involves storing a feedstock in tank with flexible walls, and introducing a plastic tunnel into an interior surface of the tank, where air pressure of the tank is 1500-3000 Pa.    USE - Method for microbiological degradation of organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a tank for microbiological degradation of organic waste.
NOVELTY - The disposer has supply pipe (70) that is connected to outlet port (17) and supplies the pressure power from outside of exhaust valve. A filter cleaning unit closes the exhaust valve and is included with processing unit. A timer (74) closes the valve for the fixed time while connecting overflow unit (18) to upper unit of the agitation vat (22). The outlet side of the water pump is installed at the upper side of the inclined surface of the bottom christou wrap. The outlet port fills the water inside the decomposition bath and overflows water reversely through the inlet port.    USE - Disposer used in dining room of home.    ADVANTAGE - The disposer can easily decompose the food waste after the fluid mixing analysis and the flooding fermentation process. The harmless in the environment is emitted in the decomposition bath. The process efficiency of the processing unit can be improved effectively. The formation of the residue in the disposer can be prevented effectively. The disposer can be easily manufactured by providing simpler structure. The maintenance of the disposer can be is facilitated and reduces the management expense. The natural environmental pollution in the disposer can be prevented effectively by ejecting the clean food waste which is adequately disassembled and processed through the processing unit.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the disposer.    Outlet port (17)    Overflow unit (18)    Agitation vat (22)    Pressure supply pipe (70)    Timer (74)
NOVELTY - Sewage sludge treatment system has primary sludge and secondary sludge thickener, container having cultured microorganism, unit for hydrolyzing sludge using the microorganism, sludge settling tank, high quality water removal tank, and second settling tank.    USE - As sewage sludge treatment system (claimed).    ADVANTAGE - The system has improved fabrication, and disposes waste easily.
NOVELTY - The apparatus has a main portion that is connected to a reservoir (100). The organic raw water stored in reservoir is processed. The organic raw water from reservoir is supplied to an acid formation tank (200) so as to separate organic waste from organic raw water. The separated organic waste from tank is supplied to a methane generating bath (300) to generate the biogas. The driving condition of tank and methane generating bath is differently controlled through a control unit. The volume of methane generating bath is set greater than the volume of tank.    USE - Two-phase anaerobic digestion apparatus used for recycling organic waste material such as food waste, food product, livestock excretion and thickened sludge for generating biogas e.g. fuel gas.    ADVANTAGE - The biogas can be produced effectively, since separated organic waste from acid formation tank is supplied to the methane generating bath for generating the biogas. The recycling efficiency of organic waste material can be improved efficiently. The production rate of biogas can be improved. The fire-extinguishing process of anaerobic digestion apparatus can be simplified. The operation condition of digestion tank can be controlled reliably. The anaerobic digestion apparatus can be operated stably. The anaerobic digestion apparatus can be maintained reliably. The economical efficiency of anaerobic digestion apparatus can be secured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the two-phase anaerobic digestion apparatus.    Reservoir (100)    Acid formation tank (200)    Methane generating bath (300)    Mixer (310)    Gas trap unit (330)
NOVELTY - Circular system for purifying livestock wastewater is claimed. The purification involves (a) isolating effective microorganisms from soil and culturing, (b) collecting livestock wastewater and inoculating cultured microorganisms in the collected wastewater, (c) adding the livestock wastewater inoculated with the microorganisms to solid-liquid separator, and carrying over aerobic fermentation, (d) transferring the primary fermented product to fermentation bath, (e) collecting the secondary fermented product, and (f) transferring the fermented product to aging tank.    USE - The circular system is useful in composition for purifying livestock waste water, where the composition is useful as liquid fertilizer and growth agents of crops (all claimed).    DETAILED DESCRIPTION - Circular system for purifying livestock wastewater is claimed. The purification involves (a) isolating effective microorganisms from soil and culturing microorganism, (b) collecting livestock wastewater and inoculating 1-10 volume/volume% cultured microorganisms in the collected wastewater, (c) adding the livestock wastewater inoculated with the microorganisms to solid-liquid separator, maintaining the wastewater for a certain period of time, and carrying over aerobic fermentation, (d) transferring the primary fermented product to secondary fermentation bath, (e) collecting the secondary fermented product, and (f) transferring the secondary fermented product to aging tank. INDEPENDENT CLAIMS are included for the following:    (1) composition, comprising culture medium, in which the above-mentioned microorganism is cultured;    (2) livestock wastewater, comprising the above-mentioned composition;    (3) liquid fertilizer comprising the above-mentioned composition; and    (4) growth agents of crops, comprising the above-mentioned composition.
NOVELTY - A diesel oil composition contains base diesel oil and additive. The base diesel oil contains biodiesel. The additive contains amination or ammonolysis reaction product of maleic anhydride-oil soluble polymer grafted copolymer, and arylamine antioxidant and/or hindered phenol antioxidant.    USE - Diesel oil composition is used for improving biodiesel oxidation stability (claimed).    ADVANTAGE - The diesel oil composition has excellent oxidation stability and low-temperature fluidity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for improving biodiesel oxidation stability.
NOVELTY - Paper sludge and domestic waste are incinerated at 250-450 degrees C, moisture content is set to 80-90%, and carbonized ash is formed. The resulting product is pulverized to powder. Carboxymethyl cellulose and water are mixed to obtain coagulant. 1-1.5 L coagulant is mixed with 5 kg pulverized powder, aggregated, and subjected to hydraulic pressing and compression molding. The resulting product is demolded, cut, and processed at 200-300 degrees C for 15-30 minutes to completely remove the moisture to produce solid fuel.    USE - Preparation of solid fuel.    ADVANTAGE - The solid fuel is economically manufactured without affecting the environment. The generation of dust is reduced.    DETAILED DESCRIPTION - Paper sludge and domestic waste are incinerated in incinerator at 250-450 degrees C by externally supplying oxygen, moisture content is set to 80-90%, and carbonized ash is formed. The resulting product is pulverized to powder. Carboxymethyl cellulose used for agglomeration of powder, and water are mixed to obtain coagulant. 1-1.5 L coagulant is mixed with 5 kg pulverized powder, aggregated, and subjected to hydraulic pressing at pressure of 150-300 ton, and compression molding. The resulting product is demolded, cut, and processed in oven at 200-300 degrees C for 15-30 minutes to completely remove the moisture to produce solid fuel.
NOVELTY - Method for preparing polyhydroxyalkyanoate from saccharified solution of Hydrodictyaceae algal biomass, involves saccharifying Hydrodictyaceae algal biomass and preparing saccharified solution containing monosaccharides.    USE - The method is useful for preparing polyhydroxyalkyanoate from saccharified solution of Hydrodictyaceae algal biomass (all claimed), which is used to produce biochemical products.    ADVANTAGE - The method is cost-effective.
NOVELTY - A fuel oil is obtained by mixing 2-30% waste oil and 30-80% water-insoluble waste organic solvent.    USE - Fuel oil (claimed).    ADVANTAGE - The fuel oil has high calorific value, and enables stable recycle of waste organic solvent and oil.
NOVELTY - The method involves connecting a gas extraction port (8) of a gasification furnace (1) with a separating tower (14) through a pipeline. The lower end of separating tower is connected with an absorption tower (19) through the pipeline. A gas collecting outlet port is arranged at upper end of the absorption tower. A pump is arranged on the gasification tower. A residual oil storage device is connected with the separation tower.    USE - Method for producing clean biomass fuel gas.    ADVANTAGE - The tar can be removed effectively from the biomass fuel gas. The purity of biomass fuel gas can be improved. The clean biomass fuel gas producing structure is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for producing clean biomass fuel gas.    Gasification furnace (1)    Gas extraction port (8)    Heat exchanger (10)    Separating tower (14)    Absorption tower (19)
NOVELTY - The device has a fluidized bed gasification reactor (1) which is connected with cyclone reforming reactor (2). Returning device (4) is connected with moving-bed catalytic reactor (3). Fluidized bed gasification reactor has a slag discharging port (C). Oxygen/steam inlet (D) is provided at upper portion of cyclone reforming reactor. Moving bed catalytic reactor has a coke inlet (F) and a gas outlet (G). Dust outlet (H) is provided at lower portion of moving bed catalytic reactor. Oxygen/steam inlet (I) is provided on returning device.    USE - Device for preparing three-section biomass gasification tar with low-high heating value gas.    ADVANTAGE - The device is featured with low cost and high energy utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing three-section biomass gasification tar with low-high heating value gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing three-section biomass gasification tar.    Fluidized bed gasification reactor (1)    Cyclone reforming reactor (2)    Moving-bed catalytic reactor (3)    Returning device (4)    Slag discharging port (C)    Oxygen/steam inlets (D,I)    Coke inlet (F)    Gas outlet (G)    Dust outlet (H)
NOVELTY - A composite sludge fuel comprises 200-600 pts. wt. sludge or mud, 200-500 pts. wt. coal powder, 10-50 pts. wt. ammonium nitrate, 5-50 pts. wt. potassium permanganate, 3-40 pts. wt. ferrous sulfate and 10-40 pts. wt. sodium chloride.    USE - Composite sludge fuel (claimed).    ADVANTAGE - The composite sludge fuel is economically prepared by a simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for Preparation of composite sludge fuel, which involves taking 200-600 pts. wt. sludge or mud, 200-500 pts. wt. coal powder, 10-50 pts. wt. ammonium nitrate, 5-50 pts. wt. potassium permanganate, 3-40 pts. wt. ferrous sulfate and 10-40 pts. wt. sodium chloride, uniformly mixing, mechanically stirring at room temperature for 30 minutes, and extruding the mixture.
NOVELTY - Biomass fuel comprises 80 pts. wt. industrial pollution sludge, 5-20 pts. wt. sulfur powder, 5-20 pts. wt. carbon and 3-5 pts. wt. cotton.    USE - Biomass fuel (claimed).    ADVANTAGE - The biomass fuel has excellent stability and combustion characteristics, and is economically manufactured by simple process with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass fuel, which involves mixing industrial pollution sludge, sulfur powder and carbon, fermenting the resultant product for 5-6 days, molding, adding cotton and drying.
NOVELTY - The anti-explosion type discharging system has a feeding port (4), a cylindrical material conveying tube (3) and a sand box (5). The feeding port is arranged on the material conveying tube. The feeding port is connected to the material conveying tube and the sand box. The sand box is provided with sand whose density is higher than the density of material in the material conveying tube. The sand box is provided with a turning roller (10) and an air suction cover (6).    USE - Anti-explosion type ash discharging system for discharging ashes from biomass pyrolysis process and biomass liquefaction process.    ADVANTAGE - The anti-explosion type ash discharging system is provided, such that the sealing effect can be ensured. The continuous discharge of the biological carbon ash can be realized. The explosion protection can be provided, hence safety can be improved effectively. The pyrolysis process and biomass liquefaction process can be performed securely. The use of biomass energy can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anti-explosion type discharging system.    Cylindrical material conveying tube (3)    Feeding port (4)    Sand box (5)    Air suction cover (6)    Turning roller (10)
NOVELTY - The system has a solar energy tracking focusing biomass gasification device (1) fixed with a solar energy mirror (2), a supporting solar energy mirror bracket (4), a power supply device, a power transmission device and an electronic control unit. The solar energy mirror is connected with the mirror bracket that is provided with a tracking control device. The tracking control device controls the solar energy mirror to focus a sunshine point. A photo-thermal converter is connected with the gasification device. The gasification device is fixed between the mirror bracket and the mirror.    USE - Mobile node array point-focusing solar energy tracking biomass gasification system.    ADVANTAGE - The system effectively realizes sunshine tracking process by moving the solar energy mirror so as to improve solar energy utilization efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a mobile node array point-focusing solar energy tracking biomass gasification system.    Solar energy tracking focusing biomass gasification device (1)    Solar energy mirror (2)    Supporting solar energy mirror bracket (4)
NOVELTY - The furnace has a furnace body provided with an upper furnace body and a lower furnace body. A feeding opening is formed at a lower part of the lower furnace body. A gas outlet is formed on a top part of the upper furnace body. A lower part of an air chamber is formed with an air lock chamber and a lock opening. A lower part of the gas outlet is provided with a condensing device that is provided with a tar re-flowing device. A lower part of the tar re-flowing device is provided with a coke oil distributor that is provided with a tar re-schizolysis device.    USE - Re-schizolysis removing tar biomass gasification furnace.    ADVANTAGE - The furnace effectively utilizes heat energy so as to effectively remove tar and ash in fuel gas. The furnace realizes effective re-schizolysis process.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a re-schizolysis removing tar biomass gasification furnace.
NOVELTY - The device has base (1) whose upper portion is set with crusher (2) to crush fast growing grass, algae, wood and lichen plant. Drying machine (3) is provided to dry crushed plant granules. Conveying pumps (4,5) are provided to convey semi-finished product of raw material. Raw material tower (6) is provided to store semi-finished product of raw material. Forming machine (7) is used to extrude semi-finished product of raw material into desired shape of bar, column, block, square, round, triangle and polygon. Conveying table (8) is used to convey extruded biomass raw material.    USE - Device for preparing ethanol fuel from waste plant material.    ADVANTAGE - The ethanol fuel preparing device is provided with improved crushing efficiency, so that the ethanol fuel can be prepared effectively from waste plant material by providing crusher to crush fast growing grass, algae, wood and lichen plant, and drying machine to dry crushed plant granules.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing ethanol fuel from waste plant material.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the device for preparing ethanol fuel from waste plant material.    Base (1)    Crusher (2)    Drying machine (3)    Conveying pumps (4,5)    Raw material tower (6)    Forming machine (7)    Conveying table (8)
NOVELTY - Manufacture of socket furnace involves crushing waste wood, cleaning, removing impurity, obtaining wood with particle size of 0.05-18 mu m, drying wood chips, removing water in an amount of 5-15%, performing superheated steam treatment of wood chips at a heat treatment temperature of 200-600 degrees C, carrying out wood surface softening, melting, performing raw material active and cementing performance, mixing cotton wood sheet, forming a fuel product, cooling, and forming socket furnace by extruding.    USE - Manufacture of socket furnace (claimed).    ADVANTAGE - The method enables environmentally-friendly and efficient manufacture of socket furnace with reduced energy consumption and residue.
NOVELTY - Fuel molding method involves crushing herbal plants or woody plant raw material, cleaning, removing impurity, obtaining wood chips having particle size of 0.05-10 mu m, mixing sawdust and cotton to achieve stable thermal value and meet requirement of stable combustion, and putting in a fuel compression molding forming machine.    USE - Fuel molding method used for combustion power generation.    ADVANTAGE - The fuel molding method is carried out with reduced energy consumption and impact on environmental pollution.
NOVELTY - Method for processing of mixed fuel involves taking sludge and bagasse or wood coal discharged from factory production process, mixing in specified amount, obtaining product with specified thermal value and required stable combustion, piling, fermenting for 5-6 days, adding water, placing into a mold, and drying.    USE - Method for processing of mixed fuel used for industrial boiler, hotel, bathroom and domestic appliance.    ADVANTAGE - The method enables processing of mixed fuel having high heat value, stable structure and excellent alkali corrosion resistance with reduced impact on environmental pollution.
NOVELTY - An environmentally-friendly charcoal comprises 90-95 pts. wt. biomass waste, 3-5 pts. wt. surfactant, 3-5 pts. wt. combustion improver, 3-5 pts. wt. phosphate and 1-2 pts. wt. cotton.    USE - Environmentally-friendly charcoal (claimed).    ADVANTAGE - The charcoal is environmentally-friendly charcoal, energy-saving and economical.
NOVELTY - Manufacture of biological waste processing fuel involves drying biological waste, grinding dried product, adding coal and chemical agent, then adding coal forming raw material, adding the resultant product, refining coal powder, drying, then adding adhesive and cotton, mixing the resultant product, carrying out extrusion molding, cooling and drying.    USE - Manufacture of biological waste processing fuel (claimed).    ADVANTAGE - The method provides biological waste processing fuel having excellent stability, combustion efficiency and renewable characteristics.
NOVELTY - The system has a smoke absorbing device that is connected with an ammonia water storage and supply device and a dust separating and recycling device. The smoke absorbing device is connected with an evaporating and crystallizing apparatus. The evaporating and crystallizing apparatus is connected with a water processing device.    USE - Flue gas desulfurization system for wet spraying absorption tower used during preparation of ammonium sulfate.    ADVANTAGE - The ammonium sulfate can be produced effectively. The flue gas treating efficiency of desulfurization system can be improved efficiently. The energy consumption of desulfurization system can be reduced. The manufacturing cost of desulfurization system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a flue gas desulfurization method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the flue gas desulfurization system. (Drawing includes non-English language text)    Absorption tower (1)    Pump (2)    Ammonia water tank (3)    Ammonia water supply pump (4)    Process water pump (5)
NOVELTY - The furnace has a furnace body (5) whose upper side is provided on a lower part of a ventilating mechanism. A guiding pipe (4) is formed with a guide hole and formed as a circular ring-shaped structure. The ventilating mechanism is provided with a fan (8) and an air channel (10). The air channel is connected with a wind pipe (6) that is arranged in the furnace body. A lower part of the furnace body is connected with an electronic ignition device. The electronic ignition device is provided with an electric heating pipe.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace is simple in structure and convenient to use, and improves raw material utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace.    Guiding pipe (4)    Furnace body (5)    Wind pipe (6)    Fan (8)    Air channel (10)
NOVELTY - An ibuprofen arginine salt solution is generated by passing salt into water. The obtained ibuprofen arginine salt solution is dried by distillation or spray, to obtain ibuprofen arginine salt.    USE - Manufacture of ibuprofen arginine salt (claimed).    ADVANTAGE - The method economically provides ibuprofen arginine salt with high yield by a simple process. The ibuprofen arginine salt is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of salt solution, which involves mixing ibuprofen or water with arginine.
NOVELTY - A methanol gasoline additive is obtained by preparing pure methanol and ethanol containing 0.8 wt.% anhydrous mixed alcohol and mixing in 2-5 wt.%. The pure methanol is prepared using additive containing 20-30 wt.%. cyclohexane, 5-15 wt.% methyl ethyl ketone, 20-40 wt.% ethanol, 20-40 wt.% naphtha and 5-15 wt.% ethyl acetate. The ethanol is prepared using additive containing 20-30 wt.% cyclohexane, 5-15 wt.% methyl ethyl ketone, 20-40 wt.% naphtha and 5-15 wt.% ethyl acetate. The methanol gasoline obtained is M15-M100 methanol gasoline.    USE - Methanol gasoline additive is used as fuel for cars.    ADVANTAGE - The methanol gasoline additive is economically manufactured by simple and easy process, and has excellent energy-saving property and efficiency.
NOVELTY - Mixture comprises 65-93 wt.% of herbaceous plants, 2-8 wt.% of oil, and 5-27 wt.% of wood.    USE - The mixture is useful as a fuel in block-type thermal power stations, a biomass boiler and a basic furnace, and for producing pellets or briquettes.
NOVELTY - The system (1) has a gas output port (12) which feed hydrogen gas and oxygen gas to the air intake of the engine. A control unit which actuates the circulation pump (24). The heat is exchanged between the electrolyte and liquid coolant. The heat exchanger (22) is provided with made of a corrosion resistant material. A cooling unit (20) comprises a radiator (30) and a circulation pump which are connected to the plate type heat exchanger, such that pump liquid coolant is circulated from the plate type heat exchanger through the radiator.    USE - System for generating hydrogen gas and oxygen gas for supplying air intake of internal combustion engine mounted in vehicle (vehicle).    ADVANTAGE - The hydrogen gas and oxygen gas can be generated effectively. The manufacturing cost of the internal combustion engine can be reduced effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) vehicle; and    (2) retrofit kit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for generating hydrogen gas and oxygen gas for supplying air intake of internal combustion engine.    System for generating hydrogen gas and oxygen gas for supplying air intake of internal combustion engine (1)    Gas output port (12)    Cooling unit (20)    Heat exchanger (22)    Circulation pump (24)    Radiator (30)
NOVELTY - Purification of natural abscisic acid involves soaking natural abscisic acid crude product with solvent, then concentrating, obtaining solid, dissolving resulting solid in concentrated lye, dissolving in the solution after extraction with organic solvent cleaning, then acidifying, acidifying with an organic solvent extraction, concentrating extract under reduced pressure, recrystallizing, filtering, washing and drying. The amount of natural abscisic acid is more than 99%. The crystals have yield of 80%.    USE - Purification of natural abscisic acid (claimed).    ADVANTAGE - The method efficiently purifies natural abscisic acid with high extraction efficiency and purity, and yield of more than 80%.
NOVELTY - Tiamulin base and methanol are reacted in fumaric acid, neutralized, centrifuged, obtained crude product is added to 4-methyl-2-pentanone, heated at 40-60 degrees C under stirring condition for 90-110 minutes, cooled to -20 to -10 degrees C for 90-110 minutes, centrifuged, dried using double cone rotary vacuum dryer, such that moisture content is less than or equal to 0.5%, sieved and packed. Thus, purification of tiamulin fumarate is carried out.    USE - Purification of tiamulin fumarate (claimed).    ADVANTAGE - The method effectively provides tiamulin fumarate having high purity by environmentally-friendly process with reduced consumption of energy and high yield.
NOVELTY - Production of 5-chloro-thiophene-2-carboxylic acid involves mixing n-butyllithium and 2-chlorothiophene, reacting at less than (-30) degrees C, terminating the reaction, and collecting the resultant reaction product.    USE - Production of 5-chloro-thiophene-2-carboxylic acid used for production of rivaroxaban (claimed).    ADVANTAGE - The method efficiently provides 5-chloro-thiophene-2-carboxylic acid with high yield and reduced discharge amount of wastewater. The 5-chloro-thiophene-2-carboxylic acid is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of rivaroxaban, which involves using 5-chloro-thiophene-2-carboxylic acid as raw material.
NOVELTY - The system has a pulse-forming network and a square-wave trigger connected together through a main switch. A load is connected to an output end of a forming net. An output end of a thin film capacitor is provided with an electrode. The square-wave trigger is provided with an energy storage pulse forming line pressure circuit and a low-jitter switch. A pressing end is connected to the main switch and a low-voltage end. An energy storage pulse forming line is connected to a vibration switch and a cathode.    USE - Slurry storage tank filtration plasmapheresis adsorption purification system for an inflammatory factor.    ADVANTAGE - The system can effectively purify autologous serum. The system can filter macromolecular toxin and protein by a secondary filtering system to ensure better liver inflammatory process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a slurry storage tank filtration plasmapheresis adsorption purification system.'(Drawing includes non-English language text)'    Primary bilirubin absorber (5)    Square liquid tank (6)    Circulating pump (7)    High-pass filter (8)    Active carbon absorber (9)    Separating plasma inlet (10)    Purified serum inlet (11)    Purifying blood plasma outlet (12)    Return blood plasma outlet (13)    One-way valves (14, 15)
NOVELTY - In situ synthesis technique of acidic catalyst film involves taking the catalytic membrane comprising ceramic membrane and molecular sieve of ZSM-5, SBA-15, MCM-41; loading sulfate ion/zirconium dioxide or sulfate ion/titanium dioxide on the surface of catalytic membrane; and then using dipping method loading active precursor containing p-methyl benzene sulfonic acid, sulfuric acid, phosphoric acid and phosphotungstic acid on the catalytic membrane. The ceramic film is composed of aluminium oxide ceramic supporting body and separation membrane and has aperture of 0.01-10 microns.    USE - For synthesis of acidic catalyst film (claimed) used in continuous film catalysis reactor for preparing biodiesel, for the esterification of oil and methanol, and for ester exchange reaction.    ADVANTAGE - The acidic catalyst film obtained by the present method is environment-friendly; has high efficiency of producing bio-diesel; and produces bio-diesel with high yield (preferably 96%).    DETAILED DESCRIPTION - In situ synthesis technique of acidic catalyst film involves taking the catalytic membrane comprising ceramic membrane and molecular sieve of ZSM-5, SBA-15, MCM-41; loading sulfate ion (SO4(2-))/zirconium dioxide or SO4(2-)/titanium dioxide on the surface of catalytic membrane; and then using dipping method loading active precursor containing p-methyl benzene sulfonic acid, sulfuric acid, phosphoric acid and phosphotungstic acid on the catalytic membrane. The ceramic film is composed of aluminium oxide ceramic supporting body and separation membrane and has aperture of 0.01-10 microns. The molecular sieve is in the citric acid.
NOVELTY - A bio-oil preparing method involves sending a biomass slurry with 40-90% water and a hydrogen-donor solvent into alkali metal catalyst and a liquefaction reactor, and reacting at 250-450 degrees C for 1-180 minutes, under total pressure intensity of 5-30 MPa, to generate a liquid-solid mixed slurry and gases, followed by separating an oil phase from the liquid-solid mixed slurry, to obtain the bio-oil containing a hydrogen-poor solvent.    USE - Method for preparing bio-oil.
NOVELTY - Coffee dregs are dry-processed with a superheated steam. Thus, the recycling of coffee dregs is carried out.    USE - Recycling of coffee dregs used for fuel (claimed).    ADVANTAGE - The method provides recycled coffee dregs having high permeability, with reduced energy consumption.
NOVELTY - Producing higher alcohols from synthesis gas produced from carbonaceous materials, involves reacting carbonaceous materials in a reactor to produce an alcohol stream and carbon dioxide, separating the alcohol stream to produce a net reactor product and a methanol stream, and feeding at least a portion of the methanol stream to the reactor, where the net reactor product is depleted of methanol.    USE - The method is useful for producing higher alcohol such as ethanol, propanol and butanol from synthesis gas produced from carbonaceous material e.g. biomass (all claimed), where the higher alcohol is used as additives in fuel or as feedstocks in the production of other chemical end products.    ADVANTAGE - The method reduces cost to produce higher order alcohols, while enabling production of the higher alcohols from a wide-range of feedstocks thus improving the economics of the process at larger scale sizes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing higher alcohols from synthesis gas produced from carbonaceous materials, comprising a gasification system to receive a carbonaceous feedstock and produce a syngas feed primarily comprising carbon monoxide, dihydrogen, methane, and carbon dioxide, a reactor to receive the syngas feed and produce an alcohol stream and carbon dioxide, and a separator to receive at least a portion of the alcohol stream and carbon dioxide and produce a methanol stream and a product stream, where the reactor receives at least a portion of the methanol stream.
NOVELTY - The method involves cooling a part of gas mixture in an exchanger (19). A part of the cooled gas mixture is separated to form light-component-enriched gas, first heavy-component-enriched liquid (17) and second heavy-component-enriched liquid (13). The first liquid is sub-cooled in the exchanger, expanded to a first pressure and vaporized at the first pressure in the exchanger. The second liquid, which is not sub-cooled in the exchanger, is vaporized in the exchanger at second pressure without expanding, where the second pressure is higher than the first pressure.    USE - Method for separating gas mixture containing a heavy component such as carbon monoxide, carbon dioxide and a light component such as hydrogen, nitrogen, oxygen, argon or methane at sub-ambient temperature.    ADVANTAGE - The part of the cooled gas mixture is separated to form the light-component-enriched gas, the first heavy-component-enriched liquid and the second heavy-component-enriched liquid, thus separating the gas mixture containing heavy component and the light component and optimizing energy consumption during separation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for separating a gas mixture containing heavy component and light component at sub-ambient temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for separating a gas mixture containing heavy component and light component at sub-ambient temperature.    Liquid part (3)    Separator phases (5A)    Liquid tank (9)    Heavy-component-enriched liquids (13, 17)    Exchanger (19)
NOVELTY - The ship (10) has an electrolysis unit that is provided in the front-end portion of a water storage pipe so that the cold seawater is electrolyzed. A high-pressure hydrogen tank (27) is provided so that storage becomes possible by a high voltage. A hydrogen recovery tube (28) recovers the hydrogen which generates by the electrolysis unit. A thermal-energy-conversion unit (17) is comprised so that thermal energy conversion is performed using a temperature difference with the cold seawater which flows through the drain tube, and the warm seawater of sea surface vicinity.    USE - Thermal-energy-conversion ship.    ADVANTAGE - The thermal-energy-conversion ship using seawater can suppress installation cost. The electric power generation efficiency can be improved. The shake of the ship main unit can be suppressed. The ship main unit can be made to navigate stably. The propulsion efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the thermal-energy-conversion ship.    Thermal-energy-conversion ship (10)    Ship main unit (11)    Thermal-energy-conversion unit (17)    High-pressure hydrogen tank (27)    Hydrogen recovery tube (28)
NOVELTY - The gas separation membrane comprises: a porous layered support (21); and a gas separating active layer (22), which is arranged on the porous layered support and comprises 1-100 layers of a functionalized graphene. The functionalized graphene has a carbon/oxygen content ratio of 1-9.5. A thickness of the gas separating active layer is 1 nm to 6 mu m. The gas separating active layer further comprises a crack having a width of less than or equal to 100 nm. The functionalized graphene is in the form of a flake. The porous layered support comprises a metal, a ceramic, a glass and/or a polymer.    USE - The membrane is useful in a gas separator for separating gas such as hydrogen (H2) and carbon dioxide (CO2), H2 and carbon monoxide, H2 and methane (CH4), H2 and nitrogen (N2), helium and N2, N2 and CO2 and/or CH4 and CO2 (all claimed) for industrial use.    ADVANTAGE - The gas separation membrane allows effective and economic separation of the gas, and can be manufactured in a convenient manner with high gas permeation rate and excellent selectivity, processability and modularity and without any cracks.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of preparing a gas separation membrane.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic cross sectional view of a gas separation membrane.    Porous layered support (21)    Gas separating active layer. (22)
NOVELTY - The hydrogen gas generation apparatus (1) has an electrolytic cell (3) which is provided with a case main portion (3a) and a cover portion (3b). The cover portion is provided for closing an opening (3c) of the case main portion. An electrode plate (15) is accommodated in the electrolytic cell. An electric power supply unit is provided for supplying the electric power to the electrode plate. The case main portion of the electrolytic cell is provided with a synthetic resin material having electrical insulation property.    USE - Hydrogen gas generation apparatus for supplying hydrogen gas to combustion unit e.g. incinerator using fuel oil.    ADVANTAGE - Since the case main portion of the electrolytic cell is provided with the synthetic resin material having electrical insulation property, the durability of the hydrogen gas generation apparatus can be improved and the performance of the hydrogen gas generation apparatus can be maintained over long period of time. The manufacturing cost of the hydrogen gas generation apparatus can be reduced. The insulating layer can be easily formed in the case main portion of the electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen gas generation apparatus. (Drawing includes non-English language text)    Hydrogen gas generation apparatus (1)    Electrolytic cell (3)    Case main portion (3a)    Cover portion (3b)    Opening (3c)    Electrode plate (15)
NOVELTY - Batch processing method of pyrolyzing and/or gasifying material involves heating the material in a processing chamber (10) by passing hot gas, pyrolyzing, gasifying and producing syngas and soot, and increasing the oxygen (22) content of hot gas, reacting oxygen with heated soot and forming carbon monoxide. The material is organically coated waste and organic material containing biomass, industrial waste, municipal solid water and sludge.    USE - Batch processing method of pyrolyzing and/or gasifying material used for producing syngas for syngas syndrome for producing electricity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) system for pyrolyzing material; and    (2) system for gasifying material.    DESCRIPTION OF DRAWING(S) - The drawing shows the system for pyrolyzing and gasifying material.    Processing chamber (10)    Thermal treatment chamber (16)    Burner (18)    Fuel (20)    Oxygen (22)
NOVELTY - Hydrothermal carbonization (HTC) method for the coalification of carbohydrate-containing biomass as feedstock, comprises (a) mixing the feedstock with water to form a dispersion, (b) optionally adding auxiliary substances and catalysts, (c) reacting the dispersion under HTC conditions, and (d) obtaining a moist, carbonaceous HTC product by separating the obtained solids from the water phase by a mechanical separation method. Fat or oil content of the feedstock is at least 6 wt.%, preferably at least 10 wt.% of the dry substance of the feedstock, or is adjusted to these minimum values.    USE - The HTC method is useful for the coalification of carbohydrate-containing biomass as feedstock (claimed).    ADVANTAGE - The intermittent or continuous HTC method supplies the product with lower residual moisture and reduced content of impurities so that drying requires less consumption of energy and without using high equipment.
NOVELTY - Digester unit comprises a digester (1) which has passage openings (7) which are sealed and are used to fill the digester with digested sludge and to empty the sludge; a heating device (9) for heating the digested sludge; at least one agitator unit (18) for agitating the digested sludge; and a gas dome (30) in which the biogas which is produced can be collected and from which the biogas to be used is further removed, where the digester is designed in the form of a standard sea container.    USE - The digester unit is useful for producing biogas from digested sludge.    ADVANTAGE - The digester unit ensures improved and cost-effective production and different usability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant comprising the digester units, where the number of digester units corresponds to the estimated performance of the biogas plant.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of the digester unit.    Digester (1)    Upper side (5)    Heating device (9)    Agitator unit (18)    Gas dome (30)
NOVELTY - Producing synthetically derived distillates using 2-5C alcohols, as feedstock involves: contacting the feed or its combinations with a zeolite type catalyst selected from a ZSM-5 or COD-9, or similar, catalyst at pressures of greater than 40 barg.    USE - For producing synthetically derived distillates using 2-5C alcohols, as feedstock (claimed). The distillates are converted into gasoline, kerosene and diesel.    ADVANTAGE - The alcohols, preferably mixed alcohols of varying chain length, is used as pure feeds or co-feeds with olefins, for the typical conversion of distillates process.
NOVELTY - Olefins and aromatic hydrocarbons are produced by supplying feed containing biomass pyrolysis-oil or fraction of biomass pyrolysis-oil to steam cracking unit operating at 600-1000 degrees C and recovering greater than or equal to 1 hydrocarbon effluent fractions.    USE - Production of olefins and aromatic hydrocarbons (claimed).    ADVANTAGE - Heat requirements for operation can be reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of olefins and aromatic hydrocarbons which involves supplying feed consisting of biomass pyrolysis oil or fraction of biomass pyrolysis oil to reverse flow reactor operating 900-1700 degrees C, recovering greater than or equal to 1 hydrocarbon effluent fractions containing acetylene, and converting a portion of acetylene to olefins and/or aromatics; and    (2) production of olefins and aromatic hydrocarbons which involves supplying feed consisting of biomass pyrolysis oil or fraction of biomass pyrolysis oil along with steam to initial heating zone at temperature sufficient to vaporize a portion of biomass pyrolysis oil in the presence of steam and produce a 2-phase stream, feeding 2-phase stream to vapor-liquid separator to produce vapor stream and liquid stream, and feeding vapor stream of to thermal cracking zone to produce product stream enriched in olefins and aromatics.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a process for upgrading biomass pyrolysis-oil by using a steam cracker.    Furnace (1)    1st tube bank (2)    Convection section (3)    1st sparger (4)    Separator vessel (5)
NOVELTY - A benzoyl pyrrole derivative (I) is new.    USE - Benzoyl pyrrole derivative (claimed).    ADVANTAGE - The benzoyl pyrrole derivative is economically prepared without polluting the environment, by a simple method.    DETAILED DESCRIPTION - A benzoyl pyrrole derivative of formula (I) is new.    R=H, alkyl, hydroxy or halo.    An INDEPENDENT CLAIM is included for manufacture of benzoyl pyrrole derivative.
NOVELTY - Composition comprises a base-treated catalyst derived from a hydroxyapatite (A), where the composition is obtained by providing an initial catalyst composition comprising (A), and treating the initial catalyst composition with a base comprising an aqueous solution of a metal hydroxide at a temperature of 25-300 degrees C and for a time of 1 minute to 24 hours.    USE - The composition is useful for producing butanol from a reactant stream including ethanol, where the butanol is useful replacing gasoline and diesel fuel, or as additives in gasoline and diesel fuel.    ADVANTAGE - The composition can provide high conversions of ethanol to butanol, and good selectivity to butanol, and has long catalytic lifetimes, thus providing higher economic benefits.    DETAILED DESCRIPTION - Composition comprises a base-treated catalyst derived from a hydroxyapatite (A) of formula ((MmManMbpMcq)5(PO4)3(OH)) (I) or ((MwMaxMbyMcz)5(PO4)3(OH)) (II), where the composition is obtained by providing an initial catalyst composition comprising (A), and treating the initial catalyst composition with a base comprising an aqueous solution of a metal hydroxide of formula (Q(OH)f) at a temperature of 25-300 degrees C and for a time of 1 minute to 24 hours.    M = Mg;    Ma = Ca;    Mb = Sr;    Mc = Ba;    Q = Li, Na, K, Rb, Cs, Sc, Y, Lu, Ti, V, Cr, Mn, Fe, Co, Ni, Cu, Zn, Zr, Nb, Mo, Ru, Rh, Pd, Ag, Hf, Ta, W, Re, Os, Ir, Pt, Au, La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, or Yb;    m, n, p, q, w, y, z = 0-1, where the sum of m+n+p+q and w+x+y+z are 1;    f = 1-3; and    x = 0 to less than 0.5.
NOVELTY - A radioactive substance containing carbohydrate-type biomass is prepared and the biomass is saccharified with enzyme and subjected to alcoholic fermentation in presence of yeast to obtain ethanol. During the manufacturing process, an acid is added, and the amount of radioactive substance present in ethanol is 1/1000 or less with respect to the amount of radioactive substance present in the radioactive substance containing carbohydrate-type biomass.    USE - Manufacture of ethanol (claimed).    ADVANTAGE - The method provides ethanol with reduced amount of radioactive substance.
NOVELTY - Bioreactor comprises carbon dioxide (CO2) distribution system, hydrogen (H2) distribution system, water collection system and CH collection system, where the bioreactor is loaded with porous solid support, in which at least 10% pore volume have a size resulting in water suction of 0.01-1 Bar, as compared to free water, the solid support is inoculated with methanogens, bioreactor comprises a solid phase, liquid phase and a gaseous phase, and volume of the gaseous phase is 20-80% with respect to volume of the bioreactor.    USE - As bioreactor.    ADVANTAGE - The bioreactor is cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for generating methane by solid state fermentation, involves (a) providing the above-mentioned bioreactor, (b) feeding CO2 and H2 into the reactor, (c) anaerobically bioconverting the CO2 and H2 into methane and water, and (d) collecting methane from the bioreactor; and    (2) use of a solid support, comprising particles having a diameter of 0.1-10 mm for at least 20% of the particles, spongy structure material having a pore size of 0.1-10 mm for at least 10% of its pores, or filamentous structure material, where the diameter of inter-filamentous spaces is 0.1-10 mm for at least 10% of its inter-filamentous spaces, or their mixture thereof for generating methane from carbon dioxide and hydrogen in a solid state fermentation process.
NOVELTY - A material having preset water content is provided and encapsulated in non-porous hydrophilic membranes (4) which absorb water molecules and transport across the non-porous hydrophilic membrane to obtain dehydrated material packages with water content lower than the water content of the material.    USE - Dehydration of material e.g. human waste, animal waste and carbon-based waste material/liquid used to produce electric power, liquid fuel, gaseous fuel (all claimed) and fertilizer.    ADVANTAGE - The method enables economical dehydration of material. The fresh water obtained by dehydration process is recycled. The dehydrated material has excellent storage stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) removal of purified water from material, which involves providing material on one side of non-porous hydrophilic membrane having thickness of less than 100 microns, preferably less than 50 microns or less than 30 microns; and    (2) fuel package, which comprises a fuel mixture encapsulated in a non-porous hydrophilic membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus for manufacture of fuel pouches.    Apparatus for manufacture of fuel pouches (1)    Feed pipe (2)    Non-porous hydrophilic membrane (4)    Heated prods (5)    Pouches (7)
NOVELTY - The apparatus has an influx unit equipped in an inner side of a body portion. A bottom plane of the body portion is provided with predetermined capacity product water. An outlet part flows out air by using a heat exchanger. Another outlet part flows out the water by using a flash chamber. The water is ejected to the flash chamber. The former outlet part is positioned in two sides of an upper portion of the body portion. A fuel cell stack is positioned in an upper end side of the body portion.    USE - Apparatus for collecting product water generated in a fuel cell stack.    ADVANTAGE - The apparatus is provided with a depositing part to collect large amount of product water generated between the fuel cell stack and the heat exchanger, so that efficiency of the heat exchanger can be improved. The apparatus reduces size of an air electrode and ejects the water to the flash chamber in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for collecting product water generated in a fuel cell stack.'(Drawing includes non-English language text)'
NOVELTY - Treating a vegetal biomass comprises (a) hydrotreating a vegetal biomass in the presence of a catalyst, (b) separating the hydrotreated product obtained into an aqueous fraction and an organic fraction, (c) concentrating the aqueous fraction, (d) mixing the concentrate with the organic fraction, and (e) further treating the obtained mixture.    USE - The method is useful for treating vegetal biomass (claimed).    ADVANTAGE - The improved method allows economic, rapid and simple treatment of vegetal biomass at mild conditions compared to known methods.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a method for the hydrotreatment of vegetal biomass.    Vegetal material (1)    Upgraded mixture (4)    Organic rich phase (5)    Aqueous phase (6)    Separator. (7)
NOVELTY - A catalyst contains carbon nanotube-loaded molybdenum carbide composite material and binder.    USE - Catalyst is used for anode for manufacturing microbial fuel cell (all claimed).    ADVANTAGE - The catalyst is manufactured efficiently and economically with excellent energy output efficiency, stability and biocompatibility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) anode, which has conductive substrate and catalyst layer containing catalyst and adhesive agent, on conductive substrate;    (2) microbial fuel cell;    (3) manufacture of catalyst; and    (4) manufacture of microbial fuel cell.
NOVELTY - Adsorbent comprises modifying agent and modified biomass coke, where the modifying agent is hydrogen peroxide, zinc chloride, sodium chloride or sodium bromide.    USE - The adsorbent is useful for the removal of mercury from flue gas (claimed).    ADVANTAGE - The adsorbent has high efficiency, and is cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the adsorbent, comprising: (a) selecting agricultural biomass Forestry biomass and biomass nuts, drying the selected biomass, crushing the dried biomass, and sieving the biomass to obtain biomass particle raw material with a particle size of less than 2-3 mm; (b) performing a pyrolysis process to the raw biomass material under a nitrogen atmosphere at 400-800 degrees C for 10-30 minutes using a fixed bed pyrolysis manufacture focusing device, cooling the processed material to room temperature under a protection of nitrogen atmosphere, and grinding the cooled material into particles with a grain size of 0.3 mm to obtain biomass pyrolysis coke; (c) continuously performing a steam activation process to the biomass pyrolysis coke at 800 degrees C for 30-60 minutes under the nitrogen atmosphere and water vapor, continuously introducing nitrogen into the device, cooling the processed material to room temperature, and grinding and sieving the cooled material into grain particles with a grain size of 0.3 mm to obtain steam activation coke, where the molar ratio of the nitrogen atmosphere and water vapor 1:1; and (d) performing an impregnation modification to the obtained steam activation coke using the modifying agent.
NOVELTY - A methanol based vehicle fuel comprises 45-55 wt.% methanol, 25-30 wt.% diesel, 5-8 wt.% biphenyl, 5-8 wt.% biphenyl ether, 3-5 wt.% butyl boron, 4-5 wt.% acetone and 0.1-0.3 wt.% tea-seed oil.    USE - Methanol based vehicle fuel.    ADVANTAGE - The fuel is inexpensive, safe, better in performance and prepared in an energy-saving manner, and avoids generation of residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a methanol based vehicle fuel, which involves adding the methanol with biphenyl ether, stirring the obtained mixture, adding biphenyl, butyl boron and acetone with the mixture, stirring the mixture, adding the tea-seed oil and the diesel with the mixture, stirring the mixture, and standing the mixture for 5-10 hours to obtain a finished product.
NOVELTY - A bio-diesel extracting method involves thermally evaporating oil residue in vapor atmosphere till the oil residue is loosened. The loosened oil residue is heated in a reaction kettle, followed by draining deposited water in the kettle. The kettle is heated to produce oil-water mixed gas. The mixed gas is allowed to pass through a pipeline to enter a cooling coil pipe in a cooling tower to cool the mixed gas into an oil-water mixed solution, which is heated, followed by draining the deposited water in the tank. The resultant solution is precipitated and filtered to obtain a finished product.    USE - Method for extracting bio-diesel from oil residue.    ADVANTAGE - The method enables extracting bio-diesel with high yield and improved economic value, in a simple and easy manner.    DETAILED DESCRIPTION - A bio-diesel extracting method involves thermally evaporating oil residue in a vapor atmosphere till the oil residue to be loosened. The loosened oil residue is heated in a reaction kettle to 85-95 degrees C for 5-10 minutes, followed by draining deposited water in the reaction kettle through a drainage valve arranged at bottom of the reaction kettle. The reaction kettle is heated to 180-330 degrees C to produce oil-water mixed gas, which is allowed to pass through a pipeline to enter a cooling coil pipe in a cooling tower to cool the mixed gas into an oil-water mixed solution. The mixed solution is heated in a heating tank to 85-110 degrees C, followed by draining the deposited water in the tank. The resultant solution is precipitated and filtered to obtain a finished product.
NOVELTY - A bio-diesel preparation method involves adding 0.3-3 g micro algae powder, solid acid catalyst and methanol into a reactor. A pre-esterification reaction is carried out at 60 plus minus 1 degrees C in a water bath for 40-60 minutes. The reaction is stopped, and the solid acid catalyst is filtered by a separating funnel. Alkaline catalyst and methanol are added to the reactor to carry out the esterification reaction at 60 plus minus 1 degrees C in the water bath for 60-80 minutes. 2-10 ml n-hexane is added to an extract in the reactor to obtain bio-diesel.    USE - Two-step catalytic conversion method for preparing bio-diesel.    ADVANTAGE - The method enables preparing bio-diesel with improved yield and shortened reaction time, in a simple and efficient manner.
NOVELTY - A pyrrolidine-dione-containing compound (I), is new.    USE - New pyrrolidine-dione-containing compound is used as low-temperature fluidity improver for fatty-acid methyl ester in biodiesel fuel composition (all claimed) used in winter or cold regions.    ADVANTAGE - The pyrrolidine-dione-containing compound improves the low-temperature fluidity and cold filter plugging point (CFPP) of fatty-acid methyl ester and biodiesel fuel containing fatty-acid methyl ester and light oil. The biodiesel fuel containing low-temperature fluidity improver is efficiently transported.    DETAILED DESCRIPTION - A pyrrolidine-dione-containing compound of formula (I), is new.    A1=partial structure of formula: -C(-R3)(-R1)-CH2- or -C(-R4)(A2-C(=O)-OR2)-CH2-;    R=1-30C aliphatic hydrocarbyl or 6-20 aryl;    m=0.25-0.85;and    i=1-4000.    An INDEPENDENT CLAIM is included for manufacture of pyrrolidine-dione-containing compound (I).
NOVELTY - The device has fermentation device main portion that is provided with primary and secondary fermentation tanks (2,3). The primary and secondary fermentation tanks are connected with each other and are provided with fermentation chamber and fermentation cavity. The fermentation chamber and fermentation cavity are provided with spiral cutter.    USE - Roller type fermentation device.    ADVANTAGE - The fermentation device has simple structure, convenient operation, high processing efficiency, small floor area, short processing time, strong applicability and energy-saving and environment-friendly effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the roller type fermentation device.    Feeding port (1)    Primary fermentation tank (2)    Secondary fermentation tank (3)    Discharge hole (6)    Transmission device (7)
NOVELTY - Producing ethanol, comprises: breaking down feedstock to make simple sugars capable of being digested by yeast; mixing yeast with the broken down feedstock in a fermentation tank (22) at a predetermined optimum temperature; adding an alcohol additive to the mixture in the fermentation tank; and removing yeast and other solids from the fermentation tank.    USE - The method is useful for producing ethanol (claimed), which is useful as fuel.    ADVANTAGE - The method: increases the yield of ethanol; and utilizes the alcohol additive, which increases the speed of the fermentation process, and reduces the amount of time needed to heat each batch, and the number of enzymatic additives.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a method of producing ethanol.    System (10)    Cellulose delivery device (12)    Hammer mill (14)    Cooking device (16)    Fermentation tank (22)
NOVELTY - Producing a purified extract comprising 40-90% theaflavins, comprises: producing tea leaves; combining an organic solvent with the tea leaves and extracting polyphenols from the tea leaves to produce an organic stock substrate solution; producing a second batch of tea leaves; grinding the second batch of tea leaves to produce stock fermentation enzyme; combining stock substrate solution with stock fermentation enzyme to produce a fermentation mixture; fermenting the mixture to produce theaflavins; and separating theaflavins from the fermentation mixture to produce purified theaflavin extract.    USE - The method is useful for producing the purified extract of theaflavins which is useful in the composition for controlling and/or treating human physiological disorder and treating a mammal infected with Influenza virus (all claimed).    ADVANTAGE - The method: allows for enhanced production of highly pure theaflavin extract in a cost-effective and environmental friendly manner; is readily controllable and avoids problems e.g. emulsifications as in traditional processes; and provides theaflavins extract having improved solubility, taste and color, and reduced caffeine level.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the purified theaflavin extract produced by the process comprising 50-85% theaflavins; and    (2) a individual dosage composition, comprising 5-95% theaflavins in a vehicle or a dietary supplement vehicle.
NOVELTY - Converting glycerin, comprises reacting glycerin in an aqueous liquid solution of hydroxide compounds (I) whose concentration is greater than saturation concentration at room temperature, at a temperature of greater than 150 degrees C to obtain formate-, acetate-, propionate-, oxalate-, lactate-, butyrate-, valerate-, citrate-, adipate-, succinate-, malate-, and/or carbonate salt, or hydrogen gas and/or methane.    USE - The method is useful for converting glycerin.    ADVANTAGE - The method produces the product with high yield.    DETAILED DESCRIPTION - Converting glycerin, comprises reacting glycerin in an aqueous liquid solution of hydroxide compounds of formula (Me-OH) (I) whose concentration is greater than saturation concentration at room temperature, at a temperature of greater than 150 degrees C to obtain formate-, acetate-, propionate-, oxalate-, lactate-, butyrate-, valerate-, citrate-, adipate-, succinate-, malate-, and/or carbonate salt, or hydrogen gas and/or methane.    Me = alkali- and/or alkaline-earth metal.
NOVELTY - Obtaining enzymatic formulation involves adding agricultural waste feedstock (10) with a particle size in the range 0.05 to 2.00 mm in a reactor (100). A stream of water (15) is injected in the reactor to adjust the moisture content for optimum growth of filamentous fungi i.e. Aspergillus on a solid matrix (30) for 12-168 hours at 20-55 degrees C. The materials are stirred in a reactor at 150-1500 revolutions per minute.    USE - Method for obtaining enzymatic formulation used for obtaining biofuel and ethanol (all claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an enzymatic formulation system.    Agricultural waste feedstock (10)    Water (15)    Solid matrix (30)    Enzyme extract (40)    Fermentation residue (50)    Reactor (100)
NOVELTY - System for production of biofuel comprising harvesting biomass from several Sorghum hybrids with differing flowering times and producing biofuel from the biomass, comprises lignocellulose and fermentable sugars, where harvesting is staggered to provide a substantially continuous supply of the biomass and the Sorghum hybrids is produced from crossing a set of at least three different Sorghum parent lines, and the parent lines each comprising a different genotype for loci contributing to flowering time phenotype.    USE - The system is useful in production of biofuel comprising harvesting biomass from several Sorghum hybrids with differing flowering times which is useful in producing inbred Sorghum plant (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for producing an inbred Sorghum plant, involves (a) crossing a first parent Sorghum plant which is homozygous dominant for the Ma6 allele with a second parent Sorghum plant which is homozygous recessive for the Ma6 allele, (b) selfing an F1 progeny, and (c) selecting for an F2 plant homozygous dominant for the Ma6 allele; (2) Sorghum seed produced by the above-mentioned method; and (3) method for identifying the genotype of a Sorghum plant for an Ma6 allele, involves (a) obtaining a Sorghum plant, and (b) assaying the Sorghum plant for a genetic marker genetically linked to the Ma6 allele.
NOVELTY - Substituted aryl compounds (I) are new.    USE - (I) are useful for marking a petroleum hydrocarbon or a liquid biologically derived fuel (claimed) e.g. bio diesel fuel, ethanol and butanol.    ADVANTAGE - (I) are added at 0.01-20 ppm to the liquid to be marked.    DETAILED DESCRIPTION - Substituted aryl compounds of formula ((Ph3C)mAr1(GR)n) (I) are new.    Ph = phenyl;    Ar1 = aromatic ring system having 6-20C;    G = O, S, SO or SO2;    R = 1-18C alkyl substituted by at least one OH, SH, 1-18C alkoxy, CN, 4-18C heteroalkyl;    m = 1-2; and    n = 1-4.    An INDEPENDENT CLAIM is also included for marking a petroleum hydrocarbon or a liquid biologically derived fuel comprising adding at least one 0.01-20 ppm to the petroleum hydrocarbon or liquid biologically derived fuel.
NOVELTY - Preparation of (2R)-dihydroartemisinic acid or (2R)-dihydroartemisinic acid esters involves: reacting artemisinic acid or artemisinic acid esters with hydrazine and/or hydrazine hydrate under an air comprising a low concentration of oxygen.    USE - For preparation of (2R)-dihydroartemisinic acid or (2R)-dihydroartemisinic acid esters as intermediates for producing artemisinin (claimed) as antimalarial drug.    ADVANTAGE - The method uses low content of oxygen to avoid or minimize chemical oxidation reaction(s); uses simple and environmentally compatible reagents and solvents to obtain high overall yields and good purity of the products and is performed on an industrial scale; result in high yield and good regio- and diastereoselectivity.    DETAILED DESCRIPTION - Preparation of (2R)-dihydroartemisinic acid or (2R)-dihydroartemisinic acid esters of formula (I) involves: reacting artemisinic acid or artemisinic acid esters of formula (II) with hydrazine and/or hydrazine hydrate under an air comprising a low concentration of oxygen.    R1=H or linear or branched 1-6C alkyl or 3-7C cycloalkyl.
NOVELTY - This utility model claims a kind of open roller machine, the high floor a walking wheel and a walking wheel are respectively provided with two ends of the walking beam of the L-shaped, walking driving motor is fixed on the L-type walking beam and connected with the high-level walking wheel, the walking driving motor is fixed on the L-type walking beam and connected with the ground walking wheel, the large-span turning target is movably mounted on the L-shaped walking beam, the main driving motor is fixed on the L-type walking beam and is connected with the large-span turning target transmission, the utility model has the advantages as follows: the operation span, which greatly increases a turning of a work area, the energy efficiency ratio is obviously improved, greatly reduces the manufacturing cost of the machine and increases the market competitive power of the product is not limited by operation space and it is more convenient to work, but also can effectively improve the working efficiency.
NOVELTY - A composite biomass granular fuel comprises 15-20 wt.% peanut shell, 15-20 wt.% wood chip, 40-50 wt.% rice husk, 8-12 wt.% grease, 6-10 wt.% gangue powder and 0.5-1 wt.% calcium oxide.    USE - Composite biomass granular fuel for use in a biomass combustion apparatus.    ADVANTAGE - The fuel has high fuel value, and prevents formation of slag.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a composite biomass granular fuel, which involves crushing peanut shell, rice husk and wood chip into powder, adding and mixing grease, gangue powder and calcium oxide with the obtained powder, compressing, screening, and packaging the obtained mixture to prepare biomass granular fuel.
NOVELTY - A low-temperature liquefied natural gas liquid is heated in liquefied natural gas storage tank, and passed into a gas-generating unit to react with input steam and air, to generate coarsely synthesized gas. The coarsely synthesized gas is cooled, passed into rectifying separating unit, and hydrogen and nitrogen in the coarsely synthesized gas is adjusted. The obtained refined synthesized gas is passed to outside battery limit ammonic synthesis unit from tower top, waste cold recovery is performed, waste gas is conveyed, and methane and hydrogen as fuel are recycled.    USE - Synthesis of ammonia using liquefied natural gas (claimed).    DETAILED DESCRIPTION - A low-temperature liquefied natural gas liquid is heated in a liquefied natural gas storage tank through heat-exchanging unit, and passed into a gas-generating unit to react with the input steam and air, to generate coarsely synthesized gas. The coarsely synthesized gas is cooled at -170 degrees C to -185 degrees C through the heat-exchanging, passed into a rectifying separating unit, and hydrogen and nitrogen in the coarsely synthesized gas is adjusted to 73-76% and 24-26%, respectively. The obtained refined synthesized gas is passed to an outside battery limit ammonic synthesis unit from the tower top, waste cold recovery is performed on a tower bottom product, the waste gas is conveyed to a fuel system, and the methane and hydrogen as fuel are recycled.
NOVELTY - Fertilizer comprises 480-836 pts. wt. of amino acid surface active compound, 8-16 pts. wt. of amino acid chelated mineral element, 210-410 pts. wt. of weng plant nutrient element and 14-26 pts. wt. of plant active agent, where the active compound comprises active ingredient with biological activity and L-amino acids.    USE - Used as fertilizer.    ADVANTAGE - The fertilizer: is environmentally friendly; rapidly improves plant growth efficiency and quality; and has resilience property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising (1) taking 120-mesh sieve agricultural products as a substrate and then adding water in the ratio of 1:8-9, (2) mixing Aspergillus oryzae, Trichoderma harzianum, Bacillus subtilis in the ratio of 1.5-2.5:0.5-1.5:0.5-1.5 to form a composite fertilizer, and (3) adding the composite fertilizer with the agricultural products and then carry out agricultural enzymatic hydrolysis.
NOVELTY - A breeding waste and crop straw processing method involves mixing breeding waste and crop straw uniformly to form a mixture. Biogas slurry is added to mixture to achieve anaerobic fermentation, followed by moving to a livestock farm. A bottom of each culture pond is paved with crop straw, followed by adding fermentation mixture. Earthworms are evenly distributed in the culture pond. A layer of processed mixture after fermentation is paved to height of 0.45m. The earthworms are collected after a month, and the substance inside the culture pool is placed in the farmland as a fertilizer.    USE - Method for integral processing of breeding waste and crop straw by earthworms.    ADVANTAGE - The method enables processing breeding waste and crop straw with better economic benefit and ecology benefit, in an effective manner. The method enables realizing sustainable development of agriculture.    DETAILED DESCRIPTION - A breeding waste and crop straw processing method involves mixing breeding waste and crop straw uniformly according to a weight ratio of 2:1 to form a mixture. 35 wt.% biogas slurry is added to mixture for a week so as to achieve anaerobic fermentation, followed by moving to a livestock farm, where length of the farm is 3m, width is 2m, and height is 0.5m. The bottom of each culture pond is paved with crop straw for a height of 5 cm, followed by adding fermentation mixture, where height of the mixture inside the pond is 0.4m. 2kg earthworms are evenly distributed in the culture pond. A layer of processed mixture after fermentation is paved to a height of 0.45m. The earthworms are collected, after a month, and the substance inside the culture pool is placed in the farmland as a fertilizer.
NOVELTY - A composite microbial fertilizer comprises polyglutamate high-producing strain, complex microbial fermentation broth and nutrients, where the mass ratio of fermentation broth and composite nutrients is 1:1, the fermentation broth comprises Bacillus licheniformis, Bacillus thuringiensis, Bacillus amyloliquefaciens and Bacillus megaterium in a mass ratio of 1:1:1:1, and the complex nutrients comprise nitrogen, phosphorus, potassium, trace elements, organic matter, compound amino acid and wheat meal. An INDEPENDENT CLAIM is also included for a method for preparing a composite microbial fertilizer, which involves preparing Bacillus licheniformis, Bacillus thuringiensis, Bacillus amyloliquefaciens and Bacillus megaterium into bacteria liquid throughliquid fermentation and mixing with complex composite nutrients in a mass ratio of 1:1 to obtain the high-efficiency liquid-state composite microbial fertilizer.    USE - Composite microbial fertilizer.    ADVANTAGE - The fertilizer has water retention and fertilizer retention properties and high fertilizer efficiency, and is prepared in an eco-friendly manner with high yield.
NOVELTY - A methanol compound petrol fuel comprises 15-35% methanol, 15-45% gasoline, 20-50% coal and 0.08-2.5% antiknock additive.    USE - Methanol compound petrol fuel for motor vehicles.    ADVANTAGE - The methanol compound petrol fuel is prepared in a simple and cost-effective manner, and reduces environment pollution, reduces oil consumption and relieves energy crisis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing a methanol compound petrol fuel which involves adding methanol, petrol, coal and antiknock additive, mixing, preparing liquid slurry, uniformly suspending coal particles in the liquid, collecting coal particles in a container to release static electricity and mixing to obtain the methanol compound petrol fuel.
NOVELTY - A coal mine methane separation and purification method involves adding a certain amount of methane, adding a certain amount of nitrogen into coal mine methane, so that oxygen content of the methane is controlled below 12%, followed by pressurizing to 0.4-0.7MPa. Pressure swing adsorption process is carried out to remove nitrogen and oxygen in methane. Product gas is obtained from the adsorption phase by adopting a vacuum method.    USE - Method for separating and purifying coal mine methane in mine areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for separating and purifying coal mine methane in mine areas.'(Drawing includes non-English language text)'
NOVELTY - A livestock and poultry excrement and crop straw resources utilization method involves mixing straw livestock and poultry excrement, and adjusting solid content of the obtained mixture. An anaerobic fermentation inoculum is added to carry out anaerobic fermentation to obtain biogas residue and biogas slurry mixture. The obtained biogas is purified and taken as boiler fuel. A solid-liquid separation is carried out on the biogas residue and the biogas slurry mixture. The biogas residue, the biogas slurry mixture and straw crushing are mixed, and aerobic composting is carried out.    USE - Method for utilizing livestock and poultry excrement and crop straw resources.    ADVANTAGE - The method enables utilizing livestock and poultry excrement and crop straw resources in a simple and efficient manner.    DETAILED DESCRIPTION - A livestock and poultry excrement and crop straw resources utilization method involves mixing straw livestock and poultry excrement, and adjusting solid content of the obtained mixture to 15-40%. An anaerobic fermentation inoculum is added into the mixture to carry out anaerobic fermentation at 30-40 degrees C for 20-30 days to obtain biogas residue and biogas slurry mixture. The obtained biogas is purified and taken as boiler fuel. A solid-liquid separation is carried out on the biogas residue and the biogas slurry mixture. The biogas residue, the biogas slurry mixture and straw crushing are mixed and aerobic composting is carried out for 20-35 days.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for utilizing livestock and poultry excrement and crop straw resources.'(Drawing includes non-English language text)'
NOVELTY - A composition comprises microalgae and a suitable growth medium where the suitable growth medium comprises water, a nutritionally acceptable nitrate salt, and a carbonate salt; where the concentration of nutritionally acceptable nitrate salt is 75-200 mu M and the concentration of carbonate salt is 1-6 mM.    USE - The composition and the process are useful for making a biofuel intermediate (claimed).    ADVANTAGE - The composition and the process efficiently and effectively grow microalgae suitable for biofuel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a process for making a biofuel intermediate comprising: (1) supplying light to a suitable growth medium comprising microalgae; and (2) growing the microalgae in the suitable growth medium; where the suitable growth medium comprises water, a nutritionally acceptable nitrate salt, and a carbonate salt and where the concentration of nutritionally acceptable nitrate salt is 75-200 mu M and the concentration of carbonate salt is 1-6 mu M; and (3) harvesting the microalgae where the harvested microalgae comprise one or more of the following characteristics: (a) the microalgae yield at least 5% w/w more glucose than microalgae grown in a comparable composition lacking the carbonate salt; (b) the microalgae stably yield at least 15% w/w glucose; and (c) the microalgae yield at least 10% w/w more glucose than microalgae grown in a comparable composition with 1500 mu M of the same nitrate salt; and    (2) a growth medium package for microalgae comprising a nutritionally acceptable nitrate salt and a carbonate salt; where the ratio of nitrate to carbonate is such that when the medium package is diluted to form a suitable growth medium the concentration of nutritionally acceptable nitrate salt is 120-170 mu M and the concentration of carbonate salt is 2-5 mM.
NOVELTY - A composting appliance comprises first container capable of containing compostable materials; and first aerobic sensor to sense aerobic or anaerobic conditions of the compostable materials contained in the first container.    USE - Composting appliance, e.g. for food scraps.    ADVANTAGE - The appliance provides for synchronous initial reaction and curing phases for continuous composting.
NOVELTY - An agricultural article comprises 0.1-1000 g of fertilizer composition contained by a biodegradable film.    USE - Agricultural article for treating compost (claimed), preferably for in-home composting.    ADVANTAGE - The article is easy for customizing and convenient to consumer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a starter kit comprising a composting appliance and/or the agricultural article, and optionally instructions for administering the article to the composting appliance; and    (2) a product comprising a tub and agricultural articles.
NOVELTY - Preparing an alpha , omega -Cn-diol, where n is greater than or equal to 5, comprises (a) providing a feedstock comprising a Cn oxygenate, and (b) contacting the feedstock with hydrogen gas, in the presence of a catalyst to form a product mixture comprising alpha , omega -Cn-diol, where the catalyst comprises metals M1 consisting of manganese, chromium, vanadium, titanium, platinum or rhodium, M2 consisting of nickel, cobalt, iron, copper or palladium, and M3 consisting of copper, silver, platinum, palladium, gold, molybdenum, rhenium or tungsten, and optionally a support.    USE - The process is useful for preparing an alpha , omega -Cn-diol (claimed) such as 1,5-pentanediol and 1,6-hexanediol, which is useful as a chemical intermediate for the production of agrichemicals, pharmaceuticals, and polymers and as plasticizers.    ADVANTAGE - The process economically and efficiently prepares high yield of alpha , omega -Cn-diol from renewable biosources and biomass-derived starting materials e.g. agricultural residues, municipal solid waste, industrial solid waste, sludge from paper manufacture, yard waste, wood and forestry waste, with high selectivity.
NOVELTY - The utility model claims a kind of energy self-biological preparation system of biomass moulded fuel, comprising a biomass gasification furnace and a pressing block forming machine, further comprising a crusher and a dryer, wherein the biomass gasification furnace is connected with a gas storage cabinet, a gas storage cabinet gas supply connected to the biomass gasification furnace fuel gas generator, a gas storage cabinet gas engine, a gas storage cabinet gas of gas engine and a dryer connected to grinder is connected with the gas engine block forming machine. Using biomass raw material generate the biomass gas as energy in the preparation process, the chemical of the biomass gas can supply biomass gas through gas generator producing energy, at the same time, the chemical energy of the biomass fuel gas by gas engine directly into a high density biological fuel into mechanical drive biomass in the preparation process, system power self-supplying, it does not need external power source, energy saving and reducing consumption.
NOVELTY - This utility model claims a kind of the preparation of biologic diesel fuel system, comprising a reaction tank, further comprising a condensing device, the upper part is provided with the reaction tank are respectively connected with the inlet and outlet of the condensing device of the volatiles outlet and a return opening. A, preparing biological diesel oil, the reaction tank, the volatilization of alcohol substance to enter into the condensing device, the condensing and reflowing to the reaction tank, so as to re-participate in a reaction of the bio-diesel. This utility model claims a biologic diesel oil producing system using the condensing device in the reaction tank to volatilize the alcohol material re-liquefying, and flows back to the reaction tank so as to ensure substantially all of the alcohol as reaction material, effectively improve the actual reacting amount of alcohol to prepare raw material is completely reacted, so as to avoid the waste of alcohol substance, the pollution to the environment, the health of a, preparation amount of diesel oil, and improve the quality of the bio-diesel.
NOVELTY - Preparing ergothioneine enrich Chinese drug oral preparation, involves mixing 1 parts edible fungi mycelium, 2 parts ergothioneine, and 16 parts water at 80-100 degrees C, stirring 1-500 rotation per minute and leaching for 0.1-5 hours at pressure of 0.01-0.098MPa, concentrating for 0.01-10 hours to obtain concentrated solution; and adding food additive into the concentrated solution, and drying to prepare oral preparation.    USE - For preparing ergothioneine enrich Chinese drug oral preparation (claimed).    ADVANTAGE - The method is low cost, simple, and energy consumption production technique; and avoids yield loss.
NOVELTY - Preparation of fuel comprises taking sludge, 30-60 wt.% cassava dry grains, 2-10 wt.% calcined lime and 125-250 million high-temperature resistant aerobic bacteria, uniformly mixing, stacking and fermenting until less than or equal to 40 wt.% water content. The aerobic bacteria can withstand not greater than 50 degrees C.    USE - Method for preparing fuel (claimed).    ADVANTAGE - The fuel has 1500-1850 MJ/kg heat of combustion.
NOVELTY - This utility model claims a kind of urban biogas recycle system, comprising multiple marsh gas source, the gas source is connected with the marsh gas collecting pipe and gas centralized recovery area, said marsh gas centralized recovery section comprises a buffer, a compressor, and a storage tank, wherein the buffer with the marsh gas collecting pipe connected with the compressor is respectively connected with the buffer and storage tank. The utility model adopts structure of urban biogas recycle system, the multiple source marsh gas marsh gas and centralized recovery area connected with the marsh gas collecting pipe, the urban biogas in the large area of network collect, concentrate to realize the recycling of energy and, at the same time reduce the city pollution, avoids caused by a too high gas content, promote the urban low carbon development, and that at the same time, the device is a gas recovery, the government and environmental protection department, the development of urban biogas recycle system for the country and the society and future green energy development significance.
NOVELTY - Strengthening urban sewage oxidation ditch technique belongs to the field of sewage treatment device and denitrification. The device comprises a high voltage load active sludge reactor, a sedimentation basin, the oxidation ditch reactor and the secondary sedimentation tank. High voltage load active mud reactor is provided with anaerobic zone and aerobic zone, oxidation ditch reactor is provided with a low oxygen zone and the anoxic zone, low oxygen section for oxygen, anoxic zone propeller stirring a solution through the aeration system. At the same time the device is biological phosphorus removal of the organic matter in the sewage gathering to the sludge in the sludge for anaerobic methane production, which can promote recovery of energy in the sewage, at the same time a low oxygen and anoxic alternately to realize self-maintaining nitrogen, which can greatly reduces sewage treatment process energy consumption.
NOVELTY - The utility model claims a hydrogen preparing system, comprising a power supply device, an electrolytic bath, a hydrogen separator, separator, a purifying tower, a power supply device connected with the electrolytic cell, hydrogen separator and oxygen separators are respectively connected on the electrolytic cell, hydrogen separator and the purification tower are connected with each other. This utility model is the electrolysis hydrogen production system, the alkaline electrolytic liquid obtained by separating hydrogen, and purification tower for purifying the hydrogen to obtain hydrogen with high purity.
NOVELTY - A biomass fuel comprises 4-5 pts. wt. sawdust, 1-2 pts. wt. straw, 0.5-1 pt. wt. walnut and 0.5-1 pt. wt. bamboo.    USE - Biomass fuel.    ADVANTAGE - The fuel has stable and excellent combustion effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biomass fuel comprising weighing sawdust, straw, walnut and bamboo, crushing, drying, removing stones and wire nails, drying until 10 wt.% water, granulating, compressing and cooling.
NOVELTY - Treatment of wastewater plant sludge comprises mixing sludge and ryegrass, carrying out acid hydrolysis and carrying out anaerobic fermentation.    USE - Method for treating wastewater plant sludge used for methane production (claimed) and short chain fatty acid production.
NOVELTY - This utility model claims a up-flow type anaerobic biological film reactor, belonging to the technical field of sewage biochemical processing device. A tower body, the tower body from bottom to top is provided with a water distributing which are connected in turn, the carrier section, filling section and a three-phase separation zone, the bottom of the tower body wall is provided with a sewage inlet and a sludge inlet, is provided with a distribution vector field, the carrier section is provided with a filler section, filling section is fixedly installed with fiber filler, the filler area on the three-phase separation region provided with a three-phase separator, a three-phase separator is connected with the tower body outer wall of the three-phase separator is provided with a water outlet, the top of the three-phase separator is provided with a marsh gas outlet. This utility model has unique structure, reasonable structure, easy starting, convenient operation management, which can effectively keep the biomass, and it will not be blocked, stabilizing the biochemical effect.
NOVELTY - This utility model claims a sewage processing device, comprising a concrete building block, wherein the concrete building block provided with a cavity and the surface of the concrete building block is provided with multiple water through holes is filled with porous microorganism carrier in the cavity, a porous microorganism carrier is attached with a treated bacterin. This utility model can purify the pool water, river water, sea water and so on is contaminated; by the concrete building block is designed to rock or wood, so that at the same time the sewage treatment device further is provided with the function of beautifying the environment.
NOVELTY - An excrement treatment device, wherein it is equipped with a vertical stirring shaft, the stirring shaft is provided with a radial direction of the stirring blade in the tank body, the tank body of the power machine, the power machine is connected with the stirring shaft, the upper part of the body of the tank body is equipped with a blower, there is a feeding port, the lower part of the tank body; It solves the problem that the using anaerobic marsh gas or filling adding strain to have oxygen supplying system for garbage fermentation process, the fermentation is not complete, the problem of environment pollution, and it is widely applied to farm the animal excrement and town refuse dump processing using the human excrement and organic matter.
NOVELTY - This utility model of marsh gas power generation system, comprising multiple marsh gas fermentation tank and a marsh gas generator, marsh gas fermentation tank and the marsh gas generator is set with a marsh gas conveying pipe, wherein, the upper part close to the marsh gas conveying pipe of the marsh gas generator is provided with a drying gas, processing the biogas processor, biogas electric generator power output end is connected with the output end of the frequency conversion control cabinet, frequency conversion control cabinet is connected with a direct current output of the rectifier control cabinet, the output end of the rectifying control cabinet is connected with a direct current illuminating system. This utility model of marsh gas power generation system, it can effectively the water and sulphide in marsh gas, avoids the damage of the marsh gas generator, can effectively output the electric energy is converted into power frequency alternating current and direct current, which meets the using device of alternating current and direct current electric device to supply power. Also through solar panel, it can make the temperature of the marsh gas fermentation tank, keeping at 20 to 40 degrees centigrade, the yield of each biogas fermentation tank.
NOVELTY - A kind of kitchen garbage treatment by anaerobic fermentation system, belonging to the technical field of environment-friendly device. Wherein a feeding adjusting tank, a secondary anaerobic fermentation tank, a secondary anaerobic fermentation tank, a methane lifting type strengthening reactor, tank and a marsh gas collecting device, wherein the material feeding adjusting are respectively enter into the first grade anaerobic fermenting tank, a secondary anaerobic fermentation tank, a secondary fermentation water enter into marsh gas lifting reinforced reactor by the integration pool, a primary anaerobic fermenting tank, a secondary anaerobic fermentation tank and a methane lifting type strengthening reactor marsh gas generated by the marsh gas collecting device. The utility model is provided with a simple structure, good processing effect.
NOVELTY - Methane purifying method involves capturing carbon dioxide and hydrogen sulfide in methane using hot potassium alkali solution, an activated alcohol amine solution and an absorbent containing hydrophilic ionic liquid in supergravity separating device, and obtaining purified biogas having methane content of 95% or more, improved hot potassium alkali absorption solution rich in carbon dioxide and hydrogen sulfide, activated alcohol amine absorption solution and absorption solution containing hydrophilic ionic liquid.    USE - Methane purifying method (claimed).    ADVANTAGE - The method stably and economically provides high-purity methane having high heat value.    DETAILED DESCRIPTION - Methane purifying method involves capturing carbon dioxide and hydrogen sulfide in methane using hot potassium alkali solution, an activated alcohol amine solution and an absorbent containing hydrophilic ionic liquid in supergravity separating device, and obtaining purified biogas having methane content of 95% or more, improved hot potassium alkali absorption solution rich in carbon dioxide and hydrogen sulfide, activated alcohol amine absorption solution and absorption solution containing hydrophilic ionic liquid, releasing carbon dioxide and hydrogen sulfide from the improved hot potassium alkali absorption solution and the activated alcohol amine absorption solution at 60-80 degrees C under normal pressure to recycle the improved hot potassium alkali solution and the activated alcohol amine absorption solution, and releasing carbon dioxide and hydrogen sulfide from the absorption solution containing the hydrophilic ionic liquid at normal temperature and low pressure, to recycle the absorbent containing the hydrophilic ionic liquid. An INDEPENDENT CLAIM is included for marsh gas purifying system.
NOVELTY - Micro sample sampling tube, belonging to the technical field of medical appliance. The technical solution is as follows: the utility model comprises a test tube and a tube plug, wherein the tube plug is provided with a sampling rod, the lower end of the sampling rod is provided with a sampling ring. This utility model has simple structure, the operation is simple, saves time and energy and relieves the work difficulty of the medical staff to blood or body fluid medical detecting and sampling;
NOVELTY - An alkaline-earth metal oxide or alkaline-earth metal salt is dissolved in predetermined amount of water and stirred to form solution or suspension. The magnesium-containing industrial waste is added and calcined at 400-550 degrees C, stirred at 20-40 degrees C for 0.5-3 hours, ultrasonically-processed at 20-60 degrees C for 0.5-3 hours, dried at 70-120 degrees C, ground, calcined at 400-800 degrees C for 2-6 hours and sieved, to obtain biodiesel loading solid base catalyst.    USE - Preparation of biodiesel loading solid base catalyst (claimed).    ADVANTAGE - The biodiesel loading solid base catalyst having excellent catalytic activity is economically prepared by simple method, without environmental pollution.
NOVELTY - Microbial agent comprises Bacillus subtilis, yeast and lactic acid bacteria, where count of each microorganism is 106-107 cells/ml and total microbial count is 107-108 cells/ml.    USE - The microbial agent is useful for fermenting farmyard manure, inhibiting propagation of harmful bacteria in soil and decomposing sulfide in aquaculture water.    ADVANTAGE - The agent is cost-effective, easy to use and produced by simple method and has fast effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing the agent, which involves (a) sterilizing fermentation tank at 100-110 degrees C for 30-60 minutes, adding boiled water upto 80% vessel volume, cooling to 30-45 degrees C, sterilizing low sugar medium and high glucose medium in pressure cooker for 1-3 hours, mixing each sterilized culture medium separately with 1 l of water, adding the prepared culture mediums separately into culture vessels and stirring for 30 minutes, (b) performing aerobic culture by adding low sugar culture medium into a fermentation tank, inoculating equal amount of B.subtilis liquid, yeast liquid and lactic acid bacteria liquid, where volume of the three liquids is 4-7 l, opening filter pump for aeration, performing fermentation for 3-4 days and closing the pump when pH reaches 5-6, and (c) performing anaerobic culture by adding high glucose medium to the tank, performing culture for 3-4 days, where every 12 hours the medium is replenished and culture is completed when pH reaches 3-4.
NOVELTY - Preparation of clopidogrel synthetic intermediate-L-2-chlorophenylglycine methyl ester involves generating ortho-chlorophenylglycine by utilizing o-chlorobenzaldehyde and chloroform under the action of a phase transfer catalyst and aqueous ammonia and enabling the ortho-chlorophenylglycine to react in thionyl chloride and methanol.    USE - Preparation of clopidogrel synthetic intermediate-L-2-chlorophenylglycine methyl ester (claimed).    ADVANTAGE - The clopidogrel synthetic intermediate-L-2-chlorophenylglycine methyl ester is economically and efficiently prepared with excellent yield without polluting the environment.
NOVELTY - Promoting ryegrass primary settling sludge for producing methane, comprises (i) mixing completely the primary settling sludge and ryegrass, at 30-40 degrees C, pH value of 4-7, carrying out anaerobic fermentation under hydrolysis acid production, where the primary settling sludge and ryegrass ratio is 7:1-26:1 according to carbon-nitrogen ratio, and controlling anaerobic fermentation time to 8-16 days, and (ii) placing the mixture obtained in the step (i) at 30-40 degrees C, at the pH value of 6-8, carrying out anaerobic fermentation to produce methane, where the anaerobic fermentation time is 40-60 days.    USE - The method is useful for promoting ryegrass primary settling sludge for producing methane (claimed).    ADVANTAGE - The method can improve the dissolution of organic matter (e.g. proteins, carbohydrates, cellulose, and lignin) and hydrolysis and acidification rate to maximize short-chain fatty acid production, which can promote complete conversion of methane; reduces sludge to the environment.
NOVELTY - Residual sludge generated in a sewage treatment plant is heat-preprocessed for 15-60 minutes at 60-120 degrees C and pH is adjusted to 8-12. The sludge is left for 1-12 days in the reactor at 30-40 degrees C for anaerobic fermentation hydrolysis, and then acidified. The fermented mixture pH is set to neutral. 8-15% Anaerobic particle sludge is added and anaerobic fermentation is carried out for 6-14 days at 30-40 degrees C to produce methane.    USE - Hot-alkali combined pretreatment of residual sludge for producing methane.    ADVANTAGE - The method is environmentally-friendly, and improves dissolution of organic matter, such as protein and polysaccharide, in residual sludge, in water such that that abundant water-soluble organic matrix is provided for fermentation of sludge and generation of acid. After residual sludge is pretreated under initial alkaline condition, the dissolution and dehydration of sludge can be promoted further and short chain fatty acids can be produced continuously. Therefore, residual-sludge dehydrating efficiency and acid-generating efficiency are improved such that the yield of methane is increased to the maximum extent.
NOVELTY - Drying sludge, comprises calculating and determining original water content and heat value of the sludge and then drying and evaporating, requiring total evaporation of the T-shaped water and total weight of the sludge and generating and heating by the fermented sludge, comparing the sizes of K1 and K, determining the addition of required energy substances, adjusting cetane number ratio of the mixture by supplying water, realizing the oxygen from the mixture to dry the sludge, adding heat energy to the mixture, and increasing fermentation rate by supplying water and oxygen to the mixture.    USE - The method is useful for drying sludge (claimed).    DETAILED DESCRIPTION - Drying sludge, comprises: (a) calculating and determining original water content (Q1) and heat value (K) of the sludge and then finally drying level of the water content (Q1) to obtain the total content (T) of water and then evaporating, requiring total evaporation of the T-shaped water and total weight of the sludge and generating and heating (K1) by the fermented sludge; (b) comparing the sizes of K1 and K, and determining the addition of required energy substances is needed or not to obtain the initial formula of a fermentation mixture, adjusting cetane number (C/N) ratio of the mixture by supplying water, realizing the oxygen from the mixture to dry the sludge, adding heat energy (K2) to the mixture, and increasing fermentation rate by supplying water and oxygen to the mixture; and (c) calculating C/N value to obtained fermented mixture with an initial formulation, adjusting the C/N value of the formulation fermented mixture to 10-50, controlling the temperature and oxygen to the fermentation mixture for generating heat energy, and evaporating water content from the fermentation mixture to obtain final water content value in the sludge.
NOVELTY - Artemisinic acid is reduced to obtain dihydroartemisinic acid. Carboxy protection of the dihydroartemisinic acid is carried out and the obtained compound is oxidized using hydrogen peroxide. Catalytic rearrangement of the oxidized product is carried out to obtain artemisinin. The acid catalyzed rearrangement is carried out in the presence of 50-10000 ml organic solvent. The acid used in the reaction is Bronsted acid or Lewis acid, and the molar ratio of the acid and the dihydrogen peroxide acid derivative is 1:(1-100).    USE - Manufacture of artemisinin used in pharmaceutical composition (claimed).    ADVANTAGE - The method enables manufacture of artemisinin in high yield using inexpensive and easily available reagents, by a short synthesis route, with high selectivity. The manufacturing process is environmentally-friendly.
NOVELTY - Eucommia ulmoides raw material is ultrasonically condense-reflux extracted using an organic solvent. The extract is filtered and repeatedly extracted, and the filtrates are combined. The material is concentrated and cooled to room temperature, and a light brown extract is collected. The extract is dissolved with methanol or ethanol, ethyl acetate or chloroform solution is added, and the mixture is refluxed hot-filtered, filtrate is allowed to stand, and the precipitated crystals are filtered, washed, and dried to obtain aucubin monomer.    USE - Preparation of aucubin monomer from Eucommia ulmoides for use in medical treatment and health care applications.    ADVANTAGE - The method enables rapid, efficient, environmentally-friendly and simple industrial preparation of aucubin monomer, with low equipment requirements.    DETAILED DESCRIPTION - Eucommia ulmoides raw material is ultrasonically condense-reflux extracted using an organic solvent in a ratio of 1 kg:5-15 L at 60-95 degrees C for 0.5-2 hours. The extract is filtered and repeatedly extracted, and the filtrates are combined. The material is concentrated at 30-90 degrees C and cooled to room temperature, and a light brown extract is collected. The extract is dissolved with methanol or ethanol in a ratio of 1 kg:8-15 L, 3-6 volume times ethyl acetate or chloroform solution is added, and the mixture is refluxed for 0.5-1.5 hours and hot-filtered. The filtrate is allowed to stand at room temperature for 10-72 hours, and the precipitated crystals are filtered, washed with ethyl acetate 5 times, and dried to obtain aucubin monomer. The organic solvent is ethanol, methanol, and/or ethyl acetate.
NOVELTY - Glycyl-tyrosine is obtained by passing glycine through thionyl chloride to obtain glycyl chloride hydrochloride, and reacting glycyl chloride hydrochloride and L-tyrosine in an aqueous solution in the presence of an acid scavenger.    USE - Preparation of glycyl-tyrosine (claimed).    ADVANTAGE - The method enables economical, environmentally-friendly and simple preparation of glycyl-tyrosine with high yield.
NOVELTY - This utility model claims a kind of livestock and poultry earthworm composite enrichment device. It comprises one of a livestock and poultry breeding of livestock and poultry breeding box body, the bottom of the box body is provided with a livestock and poultry breeding grid or grid plate, the lower part of the bottom plate is connected with a breeding method of earthworm in the earthworm breeding box comprises paving soil organic matter earthworm cultivating base, the bottom of the earthworm breeding box body is provided with a ventilation passage is ventilated net, the lower part of the ventilating, air can enter the air screen, a ventilation passage provided with a oxygen supplying system for garbage fermentation of livestock manure and earthworm. The advantages are as follows: the livestock and poultry breeding does not need too much of manual processing, on one hand satisfies the demand of the growth earthworm excrement and breeding earthworm and on the other hand by the earthworm feces produced by fermentation and can be directly used as organic fertilizer, which realizes recycling of livestock breeding, which avoids the environment pollution and resource waste;
NOVELTY - Production of low-sulfur biodiesel involves adding raw oil degumming acid catalyst, catalyst and basic pH, coupling to a moisture precipitated impurities by raw oil separating apparatus, separating moisture and impurities, heating feedstock to a temperature to remove moisture, stirring reaction mixture, performing transesterification, separating biodiesel and glycerin, recovering excess heat alcohols, catalyst and acidic pH, adding water to precipitate impurities, heating to remove excess water, obtaining crude biodiesel, and distilling obtained crude biodiesel.    USE - Production of low-sulfur biodiesel (claimed).    ADVANTAGE - The low-sulfur biodiesel is economically produced with reduced sulfur content, and discharge of polluted waste gases e.g. carbon monoxide, carbon dioxide, sulfur dioxide and black smoke particles.    DETAILED DESCRIPTION - Production of low-sulfur biodiesel involves adding raw oil degumming acid catalyst, catalyst and basic pH, coupling to a moisture precipitated impurities by raw oil separating apparatus, separating moisture and impurities, heating feedstock to a temperature to remove moisture, pre-treating oil using an acid catalyst under atmospheric pressure, stirring reaction mixture, performing transesterification, heating recovery of excess alcohol to remove moisture, separating biodiesel and glycerin, recovering excess heat alcohols, catalyst and acidic pH, adding water to precipitate impurities, separating biodiesel moisture and impurities, heating to remove excess water, obtaining crude biodiesel, and distilling obtained crude biodiesel at high temperature.
NOVELTY - The reactor (100) has vertical tank casing (110) that is provided with casing inner wall and baffle plate (120). The baffle plate is connected to the casing. The inner space of casing is separated into hydrolysis acidification area (130) and methanation area (140) for generating marsh gas. The hydrolytic acidification area is formed by the baffle plate and the casing inner wall and formed around the methanation area.    USE - Two-phase integrated anaerobic digestion reactor used for treating solid organic garbage.    ADVANTAGE - Since the hydrolytic acidification area is formed by the baffle plate and the casing inner wall and formed around methanation area, the garbage is passed for hydrolysis acidification and methanation complete separation and degraded effectively. Hence the reaction efficiency and organic matter degradation rate are improved. The ratio of height to diameter of the tank portion is reduced without affecting the flow rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing method of solid organic garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the two-phase integrated anaerobic digestion reactor.    Two-phase integrated anaerobic digestion reactor (100)    Vertical tank casing (110)    Baffle plate (120)    Hydrolysis acidification area (130)    Methanation area (140)
NOVELTY - The device (1) has a main fermentation tank main portion which is provided with a material outlet (5) and a biogas outlet (3). The pre-inoculation mixing tank is provided above the main fermentation tank. The mixing tank is integrally connected with sidewall of main fermentation tank main portion. The fresh material inlet (2) is provided in the portion of pre-inoculation mixing tank. The upper portion of the mixing tank is provided with a material overflow port (4) matched with material inlet of main fermentation tank main portion.    USE - Device for producing biological fuel gas using dry anaerobic fermentation technology.    ADVANTAGE - The biological fuel gas can be produced easily and efficiently. The heat loss of the device can be reduced. The power consumption of the fermentation device can be reduced. The utilization rate of the fermentation material can be improved. The gas production rate can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for producing biological fuel gas using dry anaerobic fermentation technology.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing fuel gas.    Device for producing biological fuel gas (1)    Fresh material inlet (2)    Biogas outlet (3)    Material overflow port (4)    Material outlet (5)
NOVELTY - Preparation of aqueous liquid component involves processing solid-liquid mixture in a laminar flow reactor comprising two or more holding sections disposed below the steering at 100-300 degrees C under pressure of 0.5-7 MPa, stirring with average rate of 1-1000 m/minute, 10-500 m/minute or 30-200 m/minute, maintaining section average flow of the liquid mixture perpendicular to the horizontal plane, and adjusting residence time to two hours or more.    USE - Preparation of aqueous liquid component (claimed).    ADVANTAGE - The method efficiently and economically provides aqueous liquid component without caking and blocking.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device used for preparing aqueous liquid component.
NOVELTY - A heating pad has a bag material, an adhesion layer arranged on surface of bag material, a covering layer which peels off sticks to outer surface of adhesion layer, and a sealing layer sleeved outside the covering layer. The bag material contains heating material comprising potassium chloride, activated carbon, iron powder, water and vermiculite.    USE - Heating pad is used for the soil conditioner.    ADVANTAGE - The heating pad is environmentally-friendly, and has low heating peak temperature, and suppressed low-temperature scald phenomenon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of heating pad, which involves mixing potassium chloride, activated carbon, iron powder, water and vermiculite and molding to form bag material.
NOVELTY - Synthesis of coumarin compound involves reacting phenol and ethyl acetoacetate in molar ratio of 1:1, in presence of 2-5% multi-sulfonate acidic ionic liquid catalyst (I) at 80-110 degrees C for 50-120 minutes, and reaction pressure of one atmosphere, cooling to room temperature, and filtering, and recrystallizing the filter residue with anhydrous ethanol, and obtaining the coumarin compound. The multi-sulfonate acidic ionic liquid catalyst in the filtrate is recycled after drying and dehydrating in vacuum at 110 degrees C.    USE - Synthesis of coumarin compound (claimed).    ADVANTAGE - The method efficiently and economically provides coumarin compound, with high yield by consuming reduced amount of energy.    DETAILED DESCRIPTION - Synthesis of coumarin compound involves reacting phenol and ethyl acetoacetate in molar ratio of 1:1, in presence of 2-5% multi-sulfonate acidic ionic liquid catalyst of formula (I) at 80-110 degrees C for 50-120 minutes, and reaction pressure of one atmosphere, cooling to room temperature, and filtering, and recrystallizing the filter residue with anhydrous ethanol, and obtaining the coumarin compound. The multi-sulfonate acidic ionic liquid catalyst in the filtrate is recycled after drying and dehydrating in vacuum at 110 degrees C.    n=3 or 4.
NOVELTY - Method of extracting ginkgolide from gingko velamina involves pulverizing impurity-removed and cleaned gingko velamina to 50-80 meshes, adding compound pectinase, and performing enzymolysis to destroy gingko cell structures, such that the velamen structures are loosened, and the ginkgolide permeability is increased, and then, adding salt and ethyl acetate, extracting, filtering, concentrating, and drying.    USE - Method of extracting ginkgolide from gingko velamina (claimed).    ADVANTAGE - The method efficiently and economically extracts ginkgolide from gingko velamina having high permeability, without causing pollution to environment and without solvent residue.
NOVELTY - A kind of garbage marsh gas generating device, comprising a fermentation tank, sedimentation tank and a vacuum pump set, wherein the set composed of multiple fermentation tank so as to become, the sedimentation tank comprises multiple precipitation tank, discharge hole is connected with the vacuum pump air inlet end at last one fermentation tank bottom of the fermentation tank group is connected with the conveying pipeline, the vacuum pump air outlet end of the sedimentation tank unit in any of the fermentation tank feeding port are connected through the pipeline, is connected with the pipeline of the vacuum pump are provided with a valve. The advantages of the utility model lie in: the device has simple structure, is convenient to use, which can effectively process domestic garbage, fully uses domestic garbage as remaining value, at the same time, it prevents the environment pollution caused by waste discharge.
NOVELTY - Circular fluidizing combustion method for water coal slurry of agricultural straw coal involves grinding straw into grains using grinder, compressing straw grains into module, adding coal powder and coalification agent into compressed module for performing coalification treatment, obtaining the straw coal, processing the straw coal into water coal slurry, conveying and sowing water coal slurry into combustion chamber of suspension vulcanizing combustion boiler by slurry supplying device, combusting water coal slurry and controlling temperature in combustion chamber.    USE - Circular fluidizing combustion method for water coal slurry of agricultural straw coal (claimed).    ADVANTAGE - The circular fluidizing combustion method for water coal slurry of agricultural straw coal is efficiently enabled.    DETAILED DESCRIPTION - Circular fluidizing combustion method for water coal slurry of an agricultural straw coal involves grinding the straw into grains with grain size of 5-10 mm using a grinder, compressing the straw grains into a module with a density of 1.1-1.2 g/cm3, adding coal powder and coalification agent into the compressed module for performing coalification treatment, obtaining the straw coal, processing the straw coal into the water coal slurry, conveying and sowing the water coal slurry into a combustion chamber of a suspension vulcanizing combustion boiler by a slurry supplying device, combusting the water coal slurry and controlling the temperature in the combustion chamber at 920-990 degrees C.
NOVELTY - This utility model claims a microorganism-bound of the integrated oxidation ditch, comprising a a complete set of oxidation ditch and at least one microorganism module. The microorganism module comprises at least one microorganism component and a control unit that a part in the oxidation ditch, and comprising at least one hole is good for microorganism , the control unit is connected with the oxidation ditch, which is used for limiting the moving of the microorganism . A complete set of the oxidation ditch comprises anaerobic zone, aeration, precipitation and so on, or further comprises a slurry return mechanism. Combination part of suppression mechanism using a microorganism , location visual inherent factor of this utility new type microbial part so as to set, but also can be fixed a change factor so as to adjust, but also is capable of simple and convenient, is to create microorganism propagation and perch according to the actual use condition of the environment and effectively extend the microbe food chain in the oxidation ditch and improving the biological purification, and organisms which results in the slurry is reduced, but also can reduce the subsequent biological sludge treatment process derived from the environment.
NOVELTY - This utility model claims a kind of used for purification process of yellow wine, comprising raw material tank (1), a waste water storage tank (15), waste water cooler (3), a secondary pre-heater (4), a waste water storage tank (6), a tower (7), a pre-heater (8), a condenser III (11) and a finished product cooler (13) and a finished product tank (14), the raw material tank (1) is connected with the feeding pump (2) and the tower (7), wherein the waste water storage tank (15), a waste water cooler (3), a secondary pre-heater (4) and tower (7) are connected in turn, wherein the secondary pre-heater (4) by the waste water pump (5) is connected with the tower (7) tower top and bottom waste water pre-heating combined with a method for pre-heating the tower, to the utmost extent reduces the yellow wine is distilled during the process of heat energy consumption, producing 1 ton alcohol saturated steam consumption is only 0.4 ton, a condensing water discharging water of the sewage treatment plant without the use of water, the secondary water sewage treatment at the same time saves the water resource, so as to greatly reduce the production cost of the enterprise, simple structure, low investment cost, reduces the device energy consumption, improves the production efficiency and purifying of yellow wine alcohol concentration reach 45% (V/V), distillation rate is more than 98%.
NOVELTY - Synthesizing powdered nitric acid, comprises concentrating allantoin waste liquid to 40-50%, cooling allantoin waste liquid to 5 degrees C in a reactor, adding dilute nitric acid with a concentration of 50-65% into allantoin waste liquid under stirring conditions, controlling the molar ratio of nitric acid and urea in the reaction liquid to 1:0.9-1.1, reacting the reaction liquid at 15 degrees C for 0.5-2 hours, cooling to 5 degrees C, centrifugally separating and crystallizing, and vacuum drying the crystallized product at 50 degrees C to obtain powdered nitric acid product.    USE - The method is useful for synthesizing powdered nitric acid (claimed).    ADVANTAGE - The method comprehensively utilizes allantoin waste liquid, urea and nitric acid for the synthesis, and reduces production cost and environmental pollution (claimed).    DETAILED DESCRIPTION - Synthesizing powdered nitric acid, comprises (a) concentrating allantoin waste liquid to a concentration of 40-50%, (b) adding allantoin waste liquid into a reactor, and cooling to 5 degrees C, (c) adding dilute nitric acid with a concentration of 50-65% into allantoin waste liquid under stirring conditions, and controlling the molar ratio of nitric acid and urea in the reaction liquid to 1:0.9-1.1, (d) maintaining the reaction liquid temperature at 20 degrees C, reacting at 15 degrees C for 0.5-2 hours, cooling the reaction liquid to 5 degrees C, centrifugally separating and crystallizing, (e) vacuum drying the crystallized product at 50 degrees C to obtain powdered nitric acid product, where nitric acid content in the product is 48-50% and urea-based acetic acid impurity content is 3-5%.
NOVELTY - Processing cephalosporin bacteria dreg, comprises e.g. mixing cephalosporin bacteria residue, water and alkali, carrying out constant temperature alkaline hydrolysis reaction, carrying out solid-liquid separation process to obtain clear solution and sediment, adding clear solution into normal waste water processing system, inoculating anaerobic activated sludge in an anaerobic fermenter, mixing sediment with biological wastewater treatment sludge to obtain sediment sludge mixture, pouring sediment sludge mixture into anaerobic fermentation tank, carrying out fermentation, and stirring.    USE - The method is useful for processing cephalosporin bacteria dreg. The biogas is used as raw material for preparing organic fertilizer and as fuel (claimed).    ADVANTAGE - The method can completely eliminate bacteria cephalosporin drug residues in the slag; solves the difficulty in maintaining efficient and continuous processing of anaerobic fermentation; achieves harmless treatment; and is safe and efficient in treatment and resource utilization.    DETAILED DESCRIPTION - Processing cephalosporin bacteria dreg, comprises (i) mixing uniformly cephalosporin bacteria residue, water and alkali, carrying out constant temperature alkaline hydrolysis reaction, allowing to stand at a certain temperature, carrying out solid-liquid separation process to obtain clear solution and sediment, and adding clear solution into the normal waste water processing system for processing sediment, and (ii) inoculating anaerobic activated sludge in an anaerobic fermenter, and mixing the sediment obtained in step (i) with biological wastewater treatment sludge to obtain sediment sludge mixture, pouring sediment sludge mixture into anaerobic fermentation tank, carrying out fermentation, stirring at constant temperature in fermenting process, and intermittently discharging biogas residue and carrying out feeding operation.
NOVELTY - Acid soil carbon method involves: preparing exhausted molasses alcohol waste mash, cooling to 40 degrees c, putting Alcaligenes faecalis strain liquid waste in 0-5% mash liquid, carrying out fermentation for 8-10 m3/hour; mixing 0-5 wt.% yellow fiber single-spore Bacillus strain liquid to fresh bagasse, inoculating the fresh bagasse; mixing uniformly the obtained Alcaligenes faecalis fermented waste mash liquid with 10% filter mud and 30% bacterial bagasse, carrying out compost fermentation at 40 degrees C at pH 8 to obtain the product.    USE - Acid soil carbon method for filtering mud fermentation soil (claimed).    ADVANTAGE - The soil promotes the growth of the crop root and stem leaf; and increases crop yields.    DETAILED DESCRIPTION - Acid soil carbon method for filtering mud fermentation soil involves: preparing exhausted molasses alcohol waste mash, cooling to 40 degrees c, putting Alcaligenes faecalis strain liquid waste in 0-5% mash liquid, carrying out fermentation for 8-10 m3/hour, where the Alcaligenes faecalis fermented waste mash reaches pH 5; mixing 0-5 wt.% yellow fiber single-spore Bacillus strain liquid to fresh bagasse, inoculating the fresh bagasse; mixing uniformly the obtained Alcaligenes faecalis fermented waste mash liquid with 10% filter mud and 30% bacterial bagasse, carrying out compost fermentation at 40 degrees C at pH 8 to obtain the product.
NOVELTY - Preparing ulipristal acetate intermediate involves reacting 3-(ethylenedioxy)-21-(phenylsulfinyl)-9-demethyl-pregn-5(10),9(11),17(20),20-tetraene with an alcohol in presence of an alkali catalyst, followed by reaction with phosphite ester to form an enol ether in the form of a reaction liquid followed by adding acid and stirring.    USE - For making bisketal type intermediate compound for ulipristal acetate.    ADVANTAGE - The method is capable of avoiding a discharging process, which greatly shortens the technical route, at the same time, the technique is stable, the operation is simple, the product yield is greatly improved to more than 60%, the purity of the product is high and has wide industrial application prospect.    DETAILED DESCRIPTION - Preparing ulipristal acetate bisketal intermediate of formula (I) or (II) involves reacting 3-(ethylenedioxy)-21-(phenylsulfinyl)-9-demethyl-pregn-5(10),9(11),17(20),20-tetraene with an alcohol in presence of an alkali catalyst, at 20-70 degrees C followed by reaction with phosphite ester at 50-70 degrees C to form an enol ether reaction liquid and adding acid and stirring to obtain (I) or (II).    R1=Me, Et, n-Pr, n-Bu, i-Bu, -(CH2)4-Me, -(CH2)2CH(Me)2 or -CH2C(Me)3;    R2=-(CH2)2-, -(CH2)3-, -(C(Me)2)2- or -CH2CH(Me)-
NOVELTY - Preparing ritodrine hydrochloride comprises: (a) reacting para-benzyloxy-2-bromopropiophenone and 4-(2-aminoethyl)phenol in presence of a base to obtain para-benzyloxy-2-(2-(para-hydroxyphenyl)ethylaminopropiophenone in reaction mixture; (b) concentrating the reaction mixture; (c) adding hydrochloric acid to the concentrated mixture to obtain para-benzyloxy-2-(2-(para-hydroxyphenyl)ethylaminopropiophenone hydrochloride (II); and (d) reducing (II) to obtain ritodrine hydrochloride.    USE - The process is useful for preparation of ritodrine hydrochloride which is useful for preparing ritodrine (all claimed) that is useful to avert premature birth. No biological data given.    ADVANTAGE - The process: utilizes unprotected tyramine; and is cost-effective, simple with reduced number of steps and high yield, and environmental friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of ritodrine from ritodrine hydrochloride, comprising (a1) preparing a solution of ritodrine hydrochloride in a solvent, (b1) adding a base to the solution of ritodrine hydrochloride to obtain ritodrine, and (c1) separating the solution to obtain ritodrine.
NOVELTY - Crystalline anhydrous Form of dexlansoprazole having X-ray powder diffraction pattern, differential scanning calorimetry endotherm curve, Fourier transform infrared spectrum, and/or thermogravimetric analysis endotherm curve as given in the specification, is new.    USE - As anti-ulcer agent.    ADVANTAGE - The crystalline anhydrous Form of dexlansoprazole has improved chemical and physical properties and stability over the amorphous form, and forms with low crystallinity; exhibits improved solubility, hygroscopicity, bulk properties and/of flowability; and can be prepared using simple, cost-effective and eco-friendly method with high yield and high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a process of the preparation of crystalline anhydrous Form of dexlansoprazole; and    (2) a pharmaceutical composition comprising a storage stable crystalline anhydrous Form of dexlansoprazole having no detectable quantity of crystalline Form-I, Form-II or amorphous forms, and at least one carriers, excipients, or diluents.
NOVELTY - Organic fertilizer comprises 10-20 pts. wt. of soybean meal, 7.5-15 pts. wt. bone meal, 40-60 pts. wt. turfy soil, 30-50 pts. wt. fungus planting abandoned soil and 0.2-0.4 pts. wt. biological bacteria.    USE - As biological organic fertilizer (claimed).    ADVANTAGE - The biological organic fertilizer replaces various types of chemical fertilizer and compound fertilizer effectively, improves soil structure, enables soil to recover to original ecology and increases yield stably.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the fertilizer which involves airing and smashing, where bean pulp, turfy soil and bone meal are respectively smashed to 40-60 meshes, fermenting mixture at 45-53 degrees C for 60-90 hours by adding 5-10 wt.% water to the bean pulp, bone meal and turfy soil, mixing the raw materials, prilling the raw materials in a machine, drying, dehumidifying and packaging after being sufficiently stirred by adding 5-10 wt.% water.
NOVELTY - A decayed urea chelated fertilizer comprises 20-25 pts. wt. humic acid, 2-4 pts. wt. microbial inoculum, 40-50 pts. wt. urea, 10-15 pts. wt. bentonite, 10-15 pts. wt. zeolite powder, 2-5 pts. wt. magnesium powder, and 2-5 pts. wt. calcium powder.    USE - Decayed urea chelated fertilizer.    ADVANTAGE - The fertilizer improves soil quality and suppress nitrogen decomposition, solves the defects that seedlings are easy to burn when urea is separately used, and prolongs fertilizer efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of decayed urea chelated fertilizer comprising crushing bentonite and zeolite with particle diameter of less than 120 meshes, mixing less than 180 mesh humic acid into urea melting groove, melting urea at high temperature, stirring, chelating at 130-135 degrees C to obtain mixed slurry, reducing temperature to 100 degrees C, putting mixed slurry into granulating machine, adding less than 120 mesh magnesium powder and calcium powder, granulating, drying, adding microbial inoculum, and uniformly stirring.
NOVELTY - Vinasse effluent liquid purification involves using rotary filters to pass fluid to remove particles of size 30 mu , where recirculation of fluid is performed through sand filters to separate particles. A phase of physical-chemical action is performed for liquid to provide recirculation through the sand filters, where ozone, molecular coagulants, diallyldimethylammonium chloride homopolymers and hydrogen peroxide are injected to the product to perform chemical reaction to separate water molecules contained in filtrate. The product is separated by filtration to collect water.    USE - Method for purifying vinasse effluent liquid in continuous circulation (claimed) to obtain solid fertilizer residue, and used in waste water treatment and wine industry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a purification plant for carrying out a procedure for purification of vinasse effluent.
NOVELTY - Method for treatment and resource utilization of sludge involves injecting a catalyst and sludge with the water content of 75-90% into a reaction kettle, then injecting saturated steam with the pressure of 1.0-1.59 MPa into the reaction kettle, heating the sludge mixed with the catalyst, obtaining slurry after reaction, performing mechanical dehydration on the slurry, obtaining removing liquid and dehydrated mud cakes, and performing anaerobic digestion reaction on the removing liquid to prepare a marsh gas.    USE - Method for treatment and resource utilization of sludge (claimed).    ADVANTAGE - The method economically treats and resources utilization of sludge with improved treatment efficiency, and reduced energy consumption.
NOVELTY - Improvement of soil comprises piling up animal excrement, straw, and bran to obtain composting material; putting earthworm into composting material; breeding earthworms to obtain earthworm manure; collecting earthworm manure; air drying and crushing; uniformly spreading crushed earthworm manure on flat land surface; and turning in soil, in which earthworm manure is used at not less than 600 kg/acre.    USE - Improvement of soil (claimed).    ADVANTAGE - The method improves soil hardening and physicochemical shape of salt and alkali in soil, reduces potential of hydrogen (pH) value and salt content, improves soil fertility, and integrates alkali changing and fertility fostering. It has wide material sources, convenient to control production cost, and provides good soil improvement effect so that crops can grow very well to improved income of farmers.
NOVELTY - The improved electrolyzer is connected to a power source (3) with an electronic monitoring device (2) which controls frequency of electricity and a water circuit with a water tank (4). The water circuit has plates or electrodes (13) and gas outlet (14). A magnet (11,12) is provided for externally embracing inlet (41) and water outlet (42) at their mouths. A pump (43) is designed outside the water circuit which creates a water flow way such that the magnets guide the flow of water molecules (5) towards the electrodes.    USE - Improved electrolyzer, preferably hydrogen generator for use in automobiles.    ADVANTAGE - The improved electrolyzer is connected to a power source with an electronic monitoring device which controls frequency of electricity and a water circuit with a water tank, and thus provides good esthetic appearance in a reduced cost, and reduces fuel consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the improved electrolyzer assembly.    Electronic monitoring device (2)    Power source (3)    Water tank (4)    Water molecules (5)    Magnets (11,12)    Electrodes (13)    Gas outlet (14)    Embracing inlet (41)    Water outlet (42)    Pump (43)
NOVELTY - A system for processing waste resources, comprises a sealed tank body, where the tank body is internally composed of multiple sealed chambers which are independent, the outer walls of the multiple chambers are high-poly-material isolated layers, and each high-poly-material isolated layer is arranged between the adjacent chambers; and the upper part of the single chamber is provided with a pumping branch port and a pumping branch pipe respectively.    USE - System for processing waste resources (claimed).    ADVANTAGE - The processing system cannot cause pollution to air and soil, meanwhile, the garbage can be converted into a clean energy, the duty-cycle operation of a refuse landfill is achieved, and a problem that garbage surrounds the city is solved.    DETAILED DESCRIPTION - A system for processing waste resources, comprises a sealed tank body, where the tank body is internally composed of multiple sealed chambers which are independent, the outer walls of the multiple chambers are high-poly-material isolated layers, and each high-poly-material isolated layer is arranged between the adjacent chambers; and the upper part of the single chamber is provided with a pumping branch port and a pumping branch pipe respectively, one ends of the multiple pumping branch pipes are connected with a main pumping port in the upper part of the center of the tank body, and the main pumping port is connected with a main pumping pipe.
NOVELTY - Town sewage treatment system comprises sewage pipe (1), mechanical grid (2) connected to sewage pipe along sewage flowing direction, on-line monitoring sub-system (3), automatic spraying sub-system (4) and oxygenating sub-system (6). The on-line monitoring sub-system and automatic spraying sub-system are connected to server (5) via wired or wireless signal connection. The on-line monitoring sub-system monitors and transmits data to the server. The server controls automatic spraying sub-system.    USE - Town sewage treatment system.    ADVANTAGE - The system is inexpensive, simple in structure and ensures short processing time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of town sewage treatment system.    Sewage pipe (1)    Mechanical grid (2)    Monitoring sub-system (3)    Spraying sub-system (4)    Server (5)    Oxygenating sub-system (6)
NOVELTY - Method for preparing household garbage bacteria fertilizer, involves converting domestic garbage, processing the garbage using large winnowing vibration sieve for separating waste, conveying microorganism into vibration sieve, and fermenting the garbage into complex organic fertilizer, where the vibration sieve are 10 cm, 5 cm, and 1 cm.    USE - The method is useful for preparing household garbage bacteria fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly as it solves pollution of the domestic waste on environmental protection, cost-effective and reasonable.
NOVELTY - Deodorized fermented liquid of excrements of livestocks comprises raw materials comprising 10-18 wt.% cane molasses, 0.5-1.8 wt.% protamine, 10-20 wt.% starch, 0.6-1.5 wt.% thermophilic Lactobacillus, thermophilic Streptococcus, Saccharomyces cerevisiae, Hansenula polymorpha and anaerobic cellulose decomposition bacteria solution, and purified water (remainder).    USE - As deodorized fermented liquid of excrements of livestocks.    ADVANTAGE - The fermented liquid reduces odor of excrements of livestocks by converting cellulose into organic acid and alcohol and then into methane and carbon dioxide by anaerobic cellulose decomposition bacteria. Strains are combined with special process fermentation to increase organic matters in soil and indispensable nutrients for crops, so that the quality of crops is improved, and both production and income are increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fermented liquid, which involves adding cane molasses, protamine and starch to fermentation tank, sterilizing mixture, injecting pure water, boiling mixture at 100 degrees C, cooling mixture to 32-35 degrees C, adding the above-mentioned bacteria solution into fermentation tank, culturing for 28 days with consumption oxygen, adjusting pH to 5-5.5, and finishing fermentation process.
NOVELTY - Biological organic fertilizer is prepared from mixture by secondary biological fermentation with decomposition agent and microbial agent, where the mixture comprises castor, xylitol residue, and mushroom residue or green tea residue in ratio of 45-59:12-18:6-13:22-28, 0.2% decomposition mixture of total amount of the mixture and 0.2% microbial inoculum of total amount of the mixture.    USE - The biological organic fertilizer is useful for crops such as vegetables, and fruit trees.    ADVANTAGE - The biological organic fertilizer increases nitrogen, phosphorus, and potassium by 30-40%, organic substances by 40-50%, and beneficial microorganisms to 0.002 billion/g or higher. The method requires short production time of 10-20 days, is simple and increases yield by 10-20%, as compared to existing method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological organic fertilizer.
NOVELTY - Preparation of methacryloyloxyethyl isocyanate involves adding ethanolamine and organic solvent into reactor containing stirrer, thermometer and condensing tube, slowly dropping methyl chloroformate at 50-60 degrees C, continuously reacting for 2-4 hours, adding catalyst into the reactor, slowly dropping methylacryloyl at 80-100 degrees C, continuously reacting for 3-8 hours, adding phosphorus pentachloride into reactor, reacting at 50-100 degrees C for 48-72 hours, subjecting resulted product to solid-liquid separation, performing depressurizing, distilling the filtrate, and collecting the fraction.    USE - Preparation of methacryloyloxyethyl isocyanate used as binder.    ADVANTAGE - The methacryloyloxyethyl isocyanate is prepared with yield of more than 85 with reduced generation of toxic phosgene by environmentally-friendly method.    DETAILED DESCRIPTION - Preparation of methacryloyloxyethyl isocyanate involves adding ethanolamine and organic solvent into reactor containing stirrer, thermometer and condensing tube, slowly dropping methyl chloroformate at 50-60 degrees C, continuously reacting for 2-4 hours, adding catalyst into the reactor, slowly dropping methylacryloyl at 80-100 degrees C, continuously reacting for 3-8 hours, adding phosphorus pentachloride into reactor, reacting at 50-100 degrees C for 48-72 hours, subjecting resulted product to solid-liquid separation, performing depressurizing, distilling the filtrate, and collecting the fraction. The molar ratio of ethanolamine and methyl chloroformate is 1:1-3. The amount of catalyst added into the reactor is 0.5-3 wt.% with respect to amount of ethanolamine. The organic solvent is chosen from toluene, benzene, xylene, chlorobenzene, dichloromethane, dichloroethane and carbon tetrachloride. The catalyst is chosen from pyridine, triethylamine, dimethylformamide and dimethylsulfoxide.
NOVELTY - A maleimide-type compound (I) is new.    USE - New maleimide-type compound is useful for controlling Sclerotinia sclerotiorum or Botrytis cinerea (claimed).    ADVANTAGE - The maleimide-type compound is prepared simply, conveniently, rapidly and environmentally-friendly, can be produced in high yield and has reduced toxicity.    DETAILED DESCRIPTION - A maleimide-type compound of formula (I) is new.    R2=H or methyl;and    R1=aliphatic alkyl, phenyl optionally substituted by halo, nitro, 1-8C alkyl, 2-methyl-3-chloro, 2-methyl-5-chloro or 2-methyl-3-nitro, phenyl 1-4C linear alkyl, 1-16C linear or branched alkyl or cycloalkyl.
NOVELTY - O-phenylenediamine and phenylacetic acid in the molar ratio of 1:1-1.5 are added to reactor, reacted under protection of nitrogen, heated to 80-100 degrees C, melted, stirred, heated to 140-160 degrees C, heat-preserved for 1-4 hours, temperature is raised to 180-200 degrees C, heat-preserved for 1-4 hours, cooled to 80-100 degrees C, hot water at 80-95 degrees C is added to reactant, stirred, cooled and filtered, to obtain bendazol.    USE - Manufacture of bendazol (claimed).    ADVANTAGE - The method effectively provides bendazol with high yield of more than 90% by environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of bendazol hydrochloride, which involves adding bendazol to water, dropwise adding dilute hydrochloric acid, adjusting pH, crystallizing, filtering and drying.
NOVELTY - A composite bioorganic fertilizer comprises 1-4 pts. wt. Trichoderma viride JUWEI002 (CGMCC 7035) fermentation liquid, 1-4 pts. wt. Bacillus subtilis JUWEI001 (CGMCC 7034) fermentation liquid, 20-30 pts. wt. peat soil, 33-38 pts. wt. tobacco slag, 33-38 pts. wt. silkworm excrement, 6-7 pts. wt. calcium powder, and 1-2 pts. wt. potassium humate. The T. viride JUWEI002 has viable count of greater than or equal to 9x 108 cells/m. The B. subtilis JUWEI001 has viable count of greater than or equal to 9x 108 cells/ml.    USE - Composite bioorganic fertilizer.    ADVANTAGE - The fertilizer increases crop yield and improves crop quality and soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by uniformly mixing T. viride JUWEI002 and B. subtilis JUWEI001 fermentation liquids; hot-air-drying peat soil at 80-100 degrees C for 120 minutes; and mixing fermentation liquid mixture with sterilized peat soil, crushing and passing through 100-mesh sieve, uniformly mixing with tobacco slag, silkworm excrement, calcium powder and potassium humate, and hot-air-drying at less than 40 degrees C until water content of less than 15 wt.%.
NOVELTY - Pyrene is dissolved in an organic solvent. Dibromohydantoin is added to dissolved mixture, and reacted. The reaction mixture is filtered and recrystallized, to obtain 1-bromopyrene.    USE - Preparation of 1-bromopyrene (claimed).    ADVANTAGE - The method enables preparation of 1-bromopyrene with high yield, without environmental pollution.
NOVELTY - A methyl 14-acetyl-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadec-13-ene-5-carboxylate (A) is reacted with hydroxylamine hydrochloride and pyridine, to obtain methyl 14-((1Z)-1-(hydroxyimino)ethyl)-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadec-13-ene-5-carboxylate (B). The product is subjected to rearrangement and hydrolysis reaction, to obtain methyl 2,15-dimethyl-14-oxotetracyclo(8.7.0.02,7.011,15)heptadecane-5-carboxylate (C). The resulted product is hydrolyzed, to obtain 5-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadecan-14-one.    USE - Preparation of 5-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadecan-14-one (claimed).    ADVANTAGE - The 5-hydroxy-2,15-dimethyltetracyclo(8.7.0.02,7.011,15)heptadecan-14-one having purity of more than 98.5% is prepared with yield of more than 68% by simple, environmentally-friendly and economical process.
NOVELTY - Vegetable planting ecological fertilizer comprises 40-50 pts. wt. plant stem and leaf, 55-65 pts. wt. livestock and poultry excrement, 10-15 pts. wt. rapeseed dregs, 5-10 pts. wt. rice husk, and 10-15 pts. wt. of 10% urea solution.    USE - Vegetable planting ecological fertilizer.    ADVANTAGE - The vegetable planting ecological fertilizer has low production cost, uses wastes as raw materials, is environment-friendly, does not cause harm to vegetables even when used at excessive amount, and achieves various vegetable growth indexes of common fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vegetable planting ecological fertilizer comprising cutting the plant stem or leaf into sections, where each stem section has a length of not greater than 5 cm, mixing plant stem or leaf, livestock and poultry excrement, rapeseed dregs, and rice husk, mixing urea solution, uniformly spraying into the mixture, burying the obtained mixture into a dug pit, covering the surface with straws, and obtaining the ecological fertilizer after burying for 90 days.
NOVELTY - A spray drying tower comprises a main body (1); a cone (2) having large upper part and small lower, located at the bottom of the main body, and inserted to the bottom of the main body; a material inlet (11) located on the upper part of the main body; a hot air inlet (12); a steam outlet (21) provided on upper part of the cone; and a dehumidifying wind port and discharging port on the bottom part of the cone.    USE - A spray drying tower for producing organic fertilizer (claimed).    ADVANTAGE - The spray drying tower is environment-friendly, reduces wastewater discharge, and utilizes waste thus reducing waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of producing organic fertilizer comprising fermenting yeast, separating water from the obtained concentrate, drying water-free material using spray drying tower, purifying by subjecting to cyclone separator, adding 32-38, preferably 36.27 wt.% ammonium sulfate and 7-12, preferably 9.8 wt.% potassium sulfate to 50-55, preferably 53.93 wt.% purified material, and mixing.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a spray drying tower.    Main body (1)    Cone (2)    Material inlet (11)    Hot air inlet (12)    Steam outlet (21)
NOVELTY - Composting material reaction device comprises a full-automatic constant-temperature curing tank, which is connected with a centrifugal crushing tank provided with liquid outlet and solid outlet. The liquid outlet is connected with a sewage treatment device. The solid outlet is connected with a microwave processing device.    USE - Composting material reaction device used for integrated processing of organic material.    ADVANTAGE - The organic materials are integrally treated so that the compositing reaction time can be greatly shortened. The wastewater and material produced in the process can be completely treated in a clean and environment-friendly mode without secondary treatment. The municipal trash can be centralized and fast treated in quantity; and the growing problem about municipal trash accumulation can be solved without future trouble.
NOVELTY - Production of universal high-efficiency foliar fertilizer includes adding urea, phosphorus pentoxide, potassium hydroxide, potassium dihydrogen phosphate, and borax into a stainless steel grinder, controlling the rotation speed of the grinder, normal temperature crushing into powder, adding the powder into a stainless steel mixer, adding bacterial fermentation biological organic fertilizer alcohol, and stirring uniformly to obtain the product.    USE - Production of universal high-efficiency foliar fertilizer (claimed) used for improving the content of chlorophyll, protein, and nucleic acid in plant, promoting carbon and nitrogen metabolism of plants, and enhancing drought resistance and cold resistance of crops.    ADVANTAGE - The universal high-efficiency foliar fertilizer has good hard water resistance, wetting and spreading capability, adhesiveness, stability, solubility, and synergistic effect, can be directly diluted, dissolved, sprayed, or flushed for application to crops, enhances the absorption of water by plants and the accumulation of dry matters, and increases production and quality of crops.    DETAILED DESCRIPTION - Production of universal high-efficiency foliar fertilizer comprises providing urea having nitrogen content of 46 wt.%, 45-47% phosphorus pentoxide, 52% potassium hydroxide, 34% potassium dihydrogen phosphate, 45-47% borax, and 6% bacterial fermentation biological organic fertilizer alcohol, adding the raw materials except bacterial fermentation biological organic fertilizer alcohol into a stainless steel grinder, controlling the rotation speed of the grinder at 260-280 revolutions/minute (rpm), normal temperature crushing into powder, adding the powder into a stainless steel mixer, adding bacterial fermentation biological organic fertilizer alcohol, and stirring uniformly to obtain the product.
NOVELTY - The fermentation tank (1) has a tank body (13), a charging hole that is arranged at the top end of the tank body, and a blanking hole that is arranged at the bottom end of the tank body. A hot air emitting device is arranged in the tank body and is provided with an air inlet (22) and air outlets (21). The air inlet is connected with a blast pipe (25). The blast pipe is connected with a waste gas heat air source.    USE - Organic waste fermentation tank for processing e.g., domestic waste.    ADVANTAGE - The fermentation tank saves space, has no environmental pollution and no atmospheric pollution. Domestic waste is quickly fermented by utilizing heat seal of waste gases to carry out three-dimensional stacked gravity pressure and warming fermentation. Reduces fermentation time, shortens fermentation period and accelerates domestic waste disposal since domestic waste is decomposed by storing gravity pressure in the tank and adopting the hot air emitting device for heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the structure of the fermentation device.    Fermentation tank (1)    Tank body (13)    Air outlets (21)    Air inlet (22)    Blast pipe (25)
NOVELTY - The digester has a hot water circulator (2) arranged in a shell (10) of a methane tank (1) and provided with a hot water inlet (20) and a cold water outlet (21). A waste heat warming circulator is arranged in the tank body (30) of a cooling tank (3) and provided with a hot water outlet (40) and a cold water inlet (41). The hot water inlet is connected with the hot water outlet by a pipeline. The cold water outlet is connected with the cold water inlet by a pipeline. The hot water circulator and waste heat warming circulator have spiraly rising steel tube structures.    USE - Biogas digester for heating via water circulation.    ADVANTAGE - Waste heat of hot materials is utilized to accelerate decomposing of organic matters to promote methane to be generated quickly. Fuel coal and capital are saved, and cooling of the cooling tank is accelerated. Under low temperature condition, the methane can be generated as well even if the temperature is lower through cold and heat exchange.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a structure of the methane tank.    Methane tank (1)    Hot water circulator (2)    Cooling tank (3)    Shell (10)    Hot water inlet (20)    Cold water outlet (21)    Tank body (30)    Hot water outlet (40)    Cold water inlet (41)
NOVELTY - Biological fertilizer comprises 15-25 %mass amino acid, 5-10 %mass enzyme-containing material, 15-25 %mass fermented organic material obtained by fermenting Phellodendron seed pulp using microorganisms, and 40-60 %mass mixture of inorganic fertilizer with trace elements.    USE - As biological fertilizer in the form of powder, spherical shape, irregular solid particles, liquid fertilizer or water-soluble fertilizer (claimed).    ADVANTAGE - The fertilizer improves growth of crops, improves soil enzyme activity and crop quality, and provides nutrition to crops. The degradation rates of urea, phosphates, and biological potassium are increased with an enzyme catalysis effect of the soil enzyme, hence the fertilizer utilization rate is increased.    DETAILED DESCRIPTION - Biological fertilizer comprises 15-25 %mass amino acid, 5-10 %mass enzyme-containing material, 15-25 %mass fermented organic material obtained by fermenting Phellodendron seed pulp using microorganisms, and 40-60 %mass mixture of inorganic fertilizer with trace elements. The fertilizer is prepared by (i) obtaining animal and plant protein, hydrolyzing the protein with sulfuric acid and water, adding concentrated ammonium bicarbonate to the obtained product, maintaining acidity between 4-6 pH, and adding commercially available mixtures of one or more enzyme-containing material containing one or more of urease, chitinase and/or phytase, (ii) mixing seed meal and humic acids in the mass ratio of 2:0.5-1.5, adding 40-45 %mass water to the obtained mixture, adding fungal strain to the obtained mixture, and fermenting the obtained mixture, (iii) adding the fermented material to the product obtained in step (i), adding inorganic fertilizer to the obtained mixture, and mixing the obtained mixture to obtain finished product.
NOVELTY - A composite fertilizer comprises 3-6 crushed fresh egg shells, 1 kg crushed corn straw, 750 g rice washing water, 600 g animal viscera or carcass, and 1 kg plant ash. The fertilizer is prepared by filling raw materials in container, sealing, fermenting under sunlight for 10-25 days until there is no surface bubbles, ventilating and adding 5 kg rice washing water, sealing and continuously fermenting for 5-8 days, removing dregs and pressing remaining material, filtering liquid, recrystallizing filtrate to obtain 15-20 g crystals, packaging, sealing, and storing.    USE - Composite fertilizer used for cultivating indoor flowering plants.
NOVELTY - Method for treating kitchen wastes by utilizing photosynthetic bacteria, involves performing hydrolysis acidification treatment on the kitchen wastes until the concentration of volatile fatty acid is 5000-15000 mg/l to obtain hydrolysis acidification liquid, performing solid and liquid separation on the hydrolysis acidification liquid, and adjusting the pH value of the liquid to 6.5-7.5 to obtain a pretreated material.    USE - The method is useful for treating kitchen wastes by utilizing photosynthetic bacteria which is used for recycling the kitchen wastes used in preparing feed additives, water purification agents, ecological organic fertilizers or aquaculture baits (all claimed).    ADVANTAGE - The method is strong in poison resistance capability for treating the kitchen wastes, good in denitrification and high in organic matter removal capability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for culturing the photosynthetic bacteria by using the pretreated material, which involves inoculating 100-1000 mg/l photosynthetic bacteria flora in the pretreated material and culturing the photosynthetic bacteria flora for 3-5 days under conditions that the illuminance of 1500-5000 lux, and temperature of 25-35 degrees C and the dissolved oxygen concentration is 0-0.8 mg/l.
NOVELTY - A tetracycline continuous fermentation liquid membrane extraction apparatus comprises macromolecular ultrafiltration membrane separation apparatus (2), macromolecular ultrafiltration membrane separation apparatus inlet (3) and small molecular ultrafiltration membrane separation inlet (4). Ultra nanofiltration separation equipment (5) is connected to nanofiltration membrane separation equipment of concentrated liquid outlet and crystallization tank (7).    USE - Tetracycline continuous fermentation liquid membrane extraction apparatus.    ADVANTAGE - The apparatus has stable low temperature and pH value of tetracycline, increases production efficiency, product yield and product quality and reduces production cost and waste liquid discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the tetracycline continuous fermentation liquid membrane extraction process comprising cooling tetracycline broth to obtain low temperature continuous tetracycline broth; adding oxalic acid; acidifying fermentation broth through macromolecular ultrafiltration membrane separation equipment for impurity removal and filtration; bleaching filtrate in small molecular membrane separation apparatus; adding water and nanofiltering to obtain tetracycline product and oxalic acid and isolating tetracycline concentrate and acid filtrate; and feeding tetracycline to crystallization tank, precipitating and removing resulting crystals.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of tetracycline continuous fermentation liquid membrane extraction apparatus.    Macromolecular ultrafiltration membrane separation apparatus (2)    Macromolecular ultrafiltration membrane separation apparatus inlet (3)    Small molecular ultrafiltration membrane separation inlet (4)    Ultra nanofiltration separation equipment (5)    Crystallization tank (7)
NOVELTY - Preparing ropivacaine comprises preparing L-piperidine-2-carbonyl chloride from L-piperidine-2-carboxylic acid without intermediate separation, directly subjecting the material to a reaction with 2,6-dimethylaniline, and (S)-N-(2,6-dimethylphenyl)piperidine-2-carboxamide without separating intermediate, and directly subjecting the material to a reaction with bromopropane to prepare the ropivacaine.    USE - Method for preparing ropivacaine (claimed).    ADVANTAGE - The method is environment-friendly, has simplified operation, reduced cost, improved yield, and is suitable for industrial production.
NOVELTY - A Shinella zoogloeoides P5 strain (CGMCC NO: 7090), is new.    USE - The S.zoogloeoides P5 strain is useful for degrading nitrogen-containing heterocyclic compound, preferably pyridine in sewage (all claimed).    ADVANTAGE - The strain has improved degradation rate, and consumes less time to degrade pyridine in sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for degrading nitrogen-containing heterocyclic compound, which involves inoculating Shinella zoogloeoides P5 strain to culture medium containing pyridine.
NOVELTY - Treatment of night soil comprises separating solid-liquid manure, centrifuging, dewatering, performing anaerobic digestion with anaerobic microorganisms, decomposing organic matter in wastewater into methane and carbon dioxide, precipitating, separating sludge-water, separating out liquid, denitrifying, adjusting pH to 9.5-12, evaporating free ammonia, absorbing with acid solution to obtain ammonium salt, adjusting pH to 7.5-8.5, performing degradation to obtain chemical oxygen demand, biochemical oxygen demand and ammonia nitrogen, separating sludge and water, disinfecting, and discharging.    USE - Method for treating night soil (claimed).    ADVANTAGE - The method has full utilization of organic matters in the night soil, and high chemical oxygen demand removal efficiency.
NOVELTY - Ambroxol hydrochloride compound is synthesized by reacting raw material with p-amino cyclohexanol in presence of absolute ethanol and potassium hydroxide using 4-dimethylaminopyridine (DMAP) and 4-dimethylamino cyclohexanol as catalyst to form intermediate and reacting with concentrated hydrochloric acid in presence of water and glacial acetic acid using ethanol as solvent.    USE - Synthesis of ambroxol hydrochloride compound (claimed).    ADVANTAGE - Synthesis of ambroxol hydrochloride compound has short reaction route, mild reaction conditions, and low pollution, reduces impurities, solvent consumption, and cost, shortens single-batch production time, and improves yield and purity.    DETAILED DESCRIPTION - Ambroxol hydrochloride compound of formula (III) is synthesized by reacting raw material of formula (I) with p-amino cyclohexanol in presence of absolute ethanol and potassium hydroxide using 4-dimethylaminopyridine (DMAP) and 4-dimethylamino cyclohexanol as catalyst to form intermediate of formula (II) and reacting with concentrated hydrochloric acid in presence of water and glacial acetic acid using ethanol as solvent.
NOVELTY - A mepivacaine and its optical enantiomer is prepared by taking N-(2,6-dimethyl phenyl)-2-piperidinecarboxamide or an optical enantiomer as starting material, adding methylation reagent in formic acid solvent, and mixing with reducing reagent at controlled temperature.    USE - Preparation of mepivacaine and its optical enantiomer (claimed).    ADVANTAGE - Preparation process is simple and low-cost, has commercially available raw materials, sufficient source, and mild reaction conditions, and avoids use of hazardous reagent i.e. dimethyl sulfate and sodium cyanoborohydride.    DETAILED DESCRIPTION - A mepivacaine and its optical enantiomer is prepared by taking N-(2,6-dimethyl phenyl)-2-piperidinecarboxamide or an optical enantiomer as starting material, adding methylation reagent in formic acid solvent, mixing with reducing reagent at controlled temperature in which reaction is represented by formula (I). .
NOVELTY - A sulfonamide formate is synthesized by mixing 2-chloro-sulfonyl-N,N-dimethyl nicotinamide and ethyl carbamate in presence of acid-binding agent, ice bathing for 3-5 hours 0-10 degrees C, filtering, and drying.    USE - Preparation of sulfonamide formate (claimed).    ADVANTAGE - Preparation process reduces waste emission, improve operation environment, and is environment-friendly.
NOVELTY - A diaryl sulfide is synthesized by adding 8-15 mol.% halogenated aromatic hydrocarbon and copper powder to dimethyl sulfoxide solvent, stirring, adding thiourea and potassium hydroxide into mixture, stirring at room temperature for 10-30 minutes to mix in which mole ratio halogenated aromatic hydrocarbon:thiourea:potassium hydroxide is 5:2.5-3:5-10, heating and allowing to react while continuously stirring at 80-140 degrees C for 30-36 hours, cooling solution to room temperature, and adding mixture of ethyl acetate:water with volume ratio 1:1.    USE - A diaryl sulfide (claimed).    ADVANTAGE - Synthesis process is simple, efficient, stable, low cost, easy to operate, and environment-friendly, and has high product yield and purity, and product is ozone free, non-toxic, non-volatile, and low cost.    DETAILED DESCRIPTION - A diaryl sulfide of formula (I) is synthesized by adding 8-15 mol.% halogenated aromatic hydrocarbon and copper powder to dimethyl sulfoxide solvent, stirring, adding thiourea and potassium hydroxide into mixture and stirring at room temperature for 10-30 minutes to mix in which mole ratio halogenated aromatic hydrocarbon:thiourea:potassium hydroxide is 5:2.5-3:5-10, heating and allowing to react while continuously stirring at 80-140 degrees C for 30-36 hours, cooling solution to room temperature, adding mixture of ethyl acetate:water with volume ratio 1:1, filtering to remove solids, performing liquid separation to obtain aqueous phase with ethyl acetate, mixing, drying, and performing column chromatography.    R=H, Me, or F.
NOVELTY - Biogas and carbonate are prepared by crushing and sorting domestic garbage, mixing, subjecting to aerobic fermentation at 50-60 degrees C, piling and retting for 5-7 days, adjusting total solid concentration to 8-12 wt.% or 20-30 wt.%, mixing with water, subjecting to anaerobic fermentation at 33-37 degrees C or 53-57 degrees C to produce marsh gas, desulfurizing marsh gas by ferric oxide dry-type desulfuration, separating methane and carbon dioxide by alkanolamine solution decarburization and triethylene glycol dehydration, separating methane from biogas, and separating carbon dioxide.    USE - Preparation of biogas and carbonate by straw waste (claimed).    ADVANTAGE - Biogas has high purity and high heat value, greenhouse gas emission from marsh gas is reduced, preparation process is simple, and cost reduction is attained.    DETAILED DESCRIPTION - Biogas and carbonate are prepared by crushing and sorting domestic garbage, mixing, subjecting to aerobic fermentation at 50-60 degrees C, piling and retting for 5-7 days, adjusting total solid concentration to 8-12 wt.% or 20-30 wt.%, mixing with water, subjecting to anaerobic fermentation at 33-37 degrees C or 53-57 degrees C to produce marsh gas, desulfurizing marsh gas by ferric oxide dry-type desulfuration, separating methane and carbon dioxide by alkanolamine solution decarburization and triethylene glycol dehydration, separating methane from biogas, separating carbon dioxide into carbonization tower from tower bottom, and performing potassium hydroxide carbonization reaction.
NOVELTY - Preparation of vitamin B6 comprises heating 5-ethoxy-4-methyloxazole with dimethyl maleate or diethyl maleate; putting obtained product into autoclave, adding alcohol, adding Raney nickel catalyst, purging with nitrogen for 2-3 times, 3, replacing of hydrogen for 2-3 times, and carrying out catalytic hydrogenation, continuously reacting with hydrogen gas at 65-80 degrees C for 4-6 hours with pressure at 2-3 MPa, recovering alcohol under reduced pressure, cooling, and filtering; adding hydrochloric acid to adjust pH to 1-1.5 or bubbling hydrogen chloride gas until saturation; and purifying.    USE - Method for preparing vitamin B6 (claimed).    ADVANTAGE - The method is simple to operate and environment-friendly and has low cost, high product purity, high yield, and high product selectivity.    DETAILED DESCRIPTION - Preparation of vitamin B6 comprises:    (A) heating 5-ethoxy-4-methyloxazole and dimethyl maleate or diethyl maleate to 80-130 degrees C for 8-15 hours to obtain 3-hydroxy-2-methylpyridine-4,5-dicarboxylic acid dimethyl ester or 3-hydroxy-2-methylpyridine-4,5-dicarboxylic diethyl ester;    (B) putting obtained product into autoclave, adding 1-8 carbon alcohol, adding Raney nickel catalyst, purging with nitrogen for 2-3 times, 3, replacing of hydrogen for 2-3 times, and carrying out catalytic hydrogenation, continuously reacting with hydrogen gas at 65-80 degrees C for 4-6 hours with pressure at 2-3 MPa, recovering alcohol under reduced pressure, cooling, and filtering;    (C) adding hydrochloric acid to adjust pH to 1-1.5 or bubbling hydrogen chloride gas until saturation; and    (D) purifying.    The molar ratio of 5-ethoxy-4-methyloxazole dimethyl maleate or diethyl maleate is 1:1-1.2. The amount of catalyst is 7-18 wt.% obtained product in step A.
NOVELTY - Preparation of praziquantel comprises reacting beta -phenylethylamine with chloroacetyl chloride and chloroalkane to obtain amide derivative (I); reacting with glycine and 1-3 carbon alcohol to obtain amide derivative (II); reacting with cyclohexylmethyl chloride and chloroalkane to obtain carboxylic acid derivative (III); subjecting to intramolecular cyclization with or without toluene or chloroalkane to obtain piperazinedione derivative (IV); reducing with methanol, ethanol, or 1,4-dioxane to obtain piperazinone derivative (V); and subjecting to intramolecular cyclization.    USE - Method for preparing praziquantel (claimed).    ADVANTAGE - The method is environment-friendly and low cost, has up to 50% yield, and uses recyclable solvents.    DETAILED DESCRIPTION - Preparation of praziquantel comprises reacting beta -phenylethylamine with chloroacetyl chloride and chloroalkane as reaction solvent to obtain amide derivative of formula (I); reacting with glycine and 1-3 carbon alcohol as reaction solvent to obtain amide derivative of formula (II); reacting with cyclohexylmethyl chloride and chloroalkane as reaction solvent to obtain carboxylic acid derivative of formula (III); subjecting to intramolecular cyclization with or without toluene or chloroalkane as reaction solvent to obtain piperazinedione derivative of formula (IV); reducing with methanol, ethanol, or 1,4-dioxane as reaction solvent to obtain piperazinone derivative of formula (V); and subjecting to intramolecular cyclization.
NOVELTY - The utility model claims a marsh gas tank, sealing opening of the marsh gas tank is T shaped pipe, and the end of the T-shaped pipe is provided with a biogas slurry in the tank body at the opening edge of the tank body, the small opening end of the T-shaped pipe. Using this utility model, as long as the T-shaped pipe of the end bracket is inserted into the biogas in methane tank opening edge of the small opening of the T-shaped pipe end, in this way, generated is completely sealed in the space is formed in the pipe wall, and the marsh gas tank, it is not only convenient and simple.
NOVELTY - A 4-alkyl-5-formyl thiazole or 5-formyl thiazole is prepared by, in an organic solvent, forming aqueous solution of mixed phase with pH of 7-9, and under the action of catalyst, reacting sulfur-containing compound with oxidizing agent at 0-40 degrees C. The oxidant is chloride or bromide of alkaline earth metal or alkali metal. The catalyst is 2,2,6,6-tetramethyl-piperidine-1-oxyl free radical, 4-hydroxy-2,2,6,6 -tetramethyl-piperidine-1-oxyl free radical, 4-methoxy-2,2,6,6-tetramethyl-piperidine-1-oxyl free radical, or 4-(benzoyloxy)-2,2,6,6-tetramethyl-piperidine-1-oxy radicals.    USE - Method for preparation 4-alkyl-5-formyl thiazole or 5-formyl thiazole (claimed).    ADVANTAGE - The method has mild reaction conditions, uses inexpensive raw material, does not need potassium bromide catalyst, has simple post-treatment, is suitable for industrial production, is friendly to the environment, and can obtain high yield and high product purity.    DETAILED DESCRIPTION - Preparing 4-alkyl-5-formyl thiazole or 5-formyl thiazole comprises, in an organic solvent, forming aqueous solution of mixed phase with pH of 7-9, and under the action of catalyst, reacting sulfur-containing compound of formula (I) with oxidizing agent at 0-40 degrees C. The oxidant is chloride or bromide of alkaline earth metal or alkali metal. The catalyst is 2,2,6,6-tetramethyl-piperidine-1-oxyl free radical, 4-hydroxy-2,2,6,6 -tetramethyl-piperidine-1-oxyl free radical, 4-methoxy-2,2,6,6-tetramethyl-piperidine-1-oxyl free radical, or 4-(benzoyloxy)-2,2,6,6-tetramethyl-piperidine-1-oxy radicals.    R1=H or 1-3C optionally branched alkyl.
NOVELTY - A PVC rare-earth heat stabilizer comprises a rare earth compound which includes thiourea. The molar ratio of thiourea to the rare earth is 1:0.5-2.    USE - A PVC rare-earth heat stabilizer.    ADVANTAGE - The heat stabilizer is environment-friendly, and has reduced production costs and improved thermal stability and mechanical properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of PVC rare-earth heat stabilizer comprising reacting organic acid, thiourea and rare earth hydroxide into the constant temperature water bath at 60-80 degrees C for 20-50 minutes.
NOVELTY - A 2,5-dihydroxy-N-(2-hydroxyethyl)benzamide is prepared by performing condensation reaction with gentisate and ethanolamine.    USE - Method for preparing 2,5-dihydroxy-N-(2-hydroxyethyl)benzamide (claimed).    ADVANTAGE - The method is simple to operate, reduces cost and reduces environmental pollution.
NOVELTY - The invention relates to a process for stabilizing slag and ash dumps. According to the invention, the process consists of a stage of fertilization at a depth of 10...15 cm, using a fertilizer consisting of 10...25 t DM/ha of urban sludge stabilized with uptake of C, N, P nutrients and microorganisms and 1...1.5 t DM/ha of volcanic tuff with high zeolite content, in a supported form of the Tuff-Aln type, either solid or as 80% aqueous suspension, after which the fertilized fields are sown, in a pure culture system, with 100...150 kg/ha of leguminous and cereal crop seeds, at a depth of 3...5 cm, while maintaining and extending the stabilized surface.
NOVELTY - The apparatus has gauze layer (11) that is provided with the netting thread, so that water comes off if the lid (1) is opened. A food waste collection box is installed at the outside of the liquid component, so that the stored liquid manure naturally flows to the tube (5). A small pump (7) is adhered with perforation to control the water pressure of water. The gauze layer pours the water in the fertilizer box.    USE - Apparatus for cultivating plants and crops from food waste.    ADVANTAGE - The plants and crops from food waste can be easily cultivated and separate expenses necessary for cultivation using the food waste can be avoided. The environmental contamination can be prevented effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the apparatus for cultivating plants and crops from food waste.    Lid (1)    Tube (5)    Small pump (7)    Food protective cover (10)    Gauze layer (11)
NOVELTY - Carbon dioxide absorbent comprises aqueous solution of biogenic amine.    USE - The carbon dioxide absorbent is useful for removing carbon dioxide in the exhaust gas (claimed).    ADVANTAGE - The carbon dioxide absorbent enables to reduce utilization of renewable energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for removing carbon dioxide in the exhaust gas using the above-mentioned carbon dioxide absorbent which involves injecting aqueous solution of biogenic amine into reactor, discharging exhaust gas into the reactor, absorbing carbon dioxide from the exhaust gas, and separating the aqueous solution of biogenic amine and reusing the strain or enzyme contained in the aqueous solution.
NOVELTY - Manufacture of pitavastatin hemicalcium is crystalline form involves reacting pitavastatin compound (I) with calcium formate by dropping calcium formate solution to solution of the pitavastatin compound (I), and drying isolated solids.    USE - Manufacture of pitavastatin hemicalcium is crystalline form (claimed).    ADVANTAGE - The pitavastatin hemicalcium is manufactured with high yield by preventing the generation of chloride using calcium formate by simple method.    DETAILED DESCRIPTION - Manufacture of pitavastatin hemicalcium is crystalline form involves reacting pitavastatin compound of formula (I) with 0.5-1 mole of calcium formate by dropping calcium formate solution to solution of the pitavastatin compound (I), and drying isolated solids.    M=alkali metal.
NOVELTY - Method for preparing biogas, involves mixing pig ordure agricultural by-products silage and marine by-product, and anaerobically digesting the mixture.    USE - The method is useful for preparing biogas (claimed).
NOVELTY - A fuel composition comprises a base fuel, a 1-4C alcohol, and an oxygenate.    USE - Fuel composition for operating an internal combustion engine.    ADVANTAGE - The fuel composition has high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a fuel composition.
NOVELTY - Preparation of cortisone acetate, comprises taking 4-pregnene-11 alpha ,17 alpha -diol-3,20-dione (I) as raw material and mixed solution of chromic anhydride, sulfuric acid and water as oxidizing agent, carrying out oxidation in an oxidation reaction solvent, and quenching with oxidizing agent quencher to obtain 4-pregnene-17 alpha -ol-3,11,20-trione (II), then reacting (II) with iodine in an iodine reaction solvent to obtain 4-pregnene-21-iodo-17 alpha -ol-3,11,20-trione (III), reacting (III) with potassium acetate in a replacement reaction solvent to obtain 4-pregnene-17 alpha ,21-diol-3,11,20-trione-21-acetate.    USE - The method is useful for preparing cortisone acetate.    ADVANTAGE - The method: avoids use of bromine and dangerous hydrogenation reaction; improves product yield and reduces process cost; is more economical, safe and environment-friendly; and is suitable for industrial production.
NOVELTY - The reactor has a shell main portion (1). An upper portion of the shell main portion is equipped with a biomass feeding port (2). The lower portion of the shell main portion is provided with a cleaning port (3) and pyrolytic carbon and pyrolysis gas product outlet (4). The shell main portion is provided with a rotating shaft (5). The rotating shaft is provided with several rotating vanes (6). The outer shell is covered with a heat insulating layer (9).    USE - Rotary blade type biomass thermal cracking reactor.    ADVANTAGE - The temperature of the rotary blade type biomass thermal cracking reactor is increased at high speed. The heating efficiency of the rotary blade type biomass thermal cracking reactor is enhanced. The biomass material friction is improved. The service life of the rotary blade type biomass thermal cracking reactor is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the rotary blade type biomass thermal cracking reactor.    Shell main portion (1)    Biomass feeding port (2)    Cleaning port (3)    Pyrolytic carbon and pyrolysis gas product outlet (4)    Rotating shaft (5)    Rotating vane (6)    Heat insulating layer (9)
NOVELTY - The system has a fire grate provided with a tar unit, a tail ash section and a reaction section. A gas outlet is formed on a top part of the tar unit. A tail ash outlet is arranged on a bottom part of the tar unit. A side of the tail ash section is provided with a gasification medium inlet. A feeding port is arranged on an upper part of the reaction section. A cylinder shell body is arranged with multiple cooling tubes to form a tube beam, where an upper end opening of the cylindrical shell body is connected with a gas pipeline that is connected with the gas outlet.    USE - Tar removing type biomass fixed bed gasification furnace system.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a tar removing type biomass fixed bed gasification furnace system.
NOVELTY - The method involves uniformly adding and mixing catalyst agent with alkali carbonate. Mixture temperature is raised from 100 to 400 degrees Celsius by increasing the temperature of about 2 to 10 degrees Celsius per minute for 0.5 to 2h. A basic carbonate molten salt system is obtained through continuously raising the temperature of about 800 to 1200 degrees Celsius. Biomass material is added to the molten salt system. Combustible gas is obtained by continuously filling gasified gas at 200 to 400 degrees Celsius for 1 to 3h.    USE - Method for preparing biomass gas by utilizing solid organic waste.    ADVANTAGE - The method enables improving gasification efficiency and gas quality of the biomass gas, reducing molten salt solidification and improving heat efficiency of a biomass gasification process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for preparing biomass gas by utilizing solid organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gas preparing device.
NOVELTY - This utility model makes full use of the biomass fuel is efficient hot water furnace, the pipeline and is connected with a gasification chamber and a combustion chamber, a spiral dust remover, an ash hopper, a slag chamber and the combustion chamber are set in the furnace body is filled with water, the biomass fuel is gasified into combustible gas in the gasification chamber, a large amount of vaporizing burner of biomass fuel after the main combustion chamber, a main combustion chamber of the fuel gas is not completely carried out subsequent complete combustion in the second combustion chamber and third combustion chamber. And the biomass fuel is gasified, burning fully, to obtain perfect release, has scientific and reasonable structure, water in the form of heat, the heat energy; The smoke discharge in PM2.5, smoke dust, almost no black, no sulphur and toxic substance. Suitable for cell, school, hospital and hotel to supply hot water for daily life and heating in winter, but also suitable for industrial production of a coal, oil, gas and electric heating boiler water supply device to supply heat water for drying the material;
NOVELTY - A high-value bio-oil preparation method involves chipping a biomass raw material to obtain a biomass raw material slice, placing the slice in an oxygen-free environment, and baking the slice for 0.2-2 hours. The baked slice is crushed and sieved to obtain biomass particles. The biomass particles are transported to a cracking reactor and subjected to a quick pyrolysis reaction at 450-550 degrees C for 1.5-3 seconds to obtain a finished product. The obtained pyrolysis reaction tail gas is utilized to supply heat for the baking process.    USE - Method for preparing high-value bio-oil.    ADVANTAGE - The method enables preparing the bio-oil with reduced water content, oxygen content and acidity and increased heat value and energy density in a cost-effective, energy-saving and environmental-friendly manner.    DETAILED DESCRIPTION - A high-value bio-oil preparation method involves chipping a biomass raw material to obtain a biomass raw material slice with grain diameter of less than 20 cm, placing the slice in an oxygen-free environment at 220-320 degrees C, and baking the slice for 0.2-2 hours. The baked slice is crushed and sieved to obtain biomass particles with grain diameter of less than 2.36 cm. The biomass particles are transported to a cracking reactor and subjected to a quick pyrolysis reaction at 450-550 degrees C for 1.5-3 seconds to obtain a finished product. The obtained pyrolysis reaction tail gas is utilized to supply heat for the baking process.
NOVELTY - The method involves cooling water in a first section indirect heat exchanger. A biomass synthesis gas is heated at 350 to 550 degree Celsius with high temperature and pressure. The biomass synthesis gas is cooled at 100 to 300 degree Celsius and recycled in a second section indirect heat exchanger. Dust is removed in the biomass synthesis gas using washing solution. Residual dust of the biomass synthesis gas is removed using damp air flow depth dust-removing coke oil, where the dust and tar content is less in the biomass synthetic gas.    USE - High-temperature and high-pressure biomass synthesis gas cooling and purifying process.    ADVANTAGE - The method enables optimizing design by technical solution, controlling appropriate process parameters of biomass synthesis gas, recycling and purifying dust and tar and purifying the biomass synthesis gas in smooth, safety and stability manner. The method enables providing low energy consumption and high efficiency and ensuring better economical benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of illustrating a high-temperature and high-pressure biomass synthesis gas cooling and purifying process.
NOVELTY - This utility model claims a kind of household of energy-saving environment-friendly biomass fuel gas furnace, an air pre-heating box at the bottom of the furnace seat, the air inlet is connected with air pre-heating case through the right tee joint and a secondary wind pipe, the side air nozzle and the central nozzle extends into the furnace seat from the air pre-heating box. The upper end of the furnace seat is provided with the furnace waist, a furnace waist, the upper end of the central hole of the furnace head is connected with the inner side wall of inner container, the filter box position of the furnace head inner cavity, a water sealing groove is fixedly connected with the furnace wall, the upper end of the water sealing cover in the water seal tank. End is connected with the upper end of a gas pipe is respectively connected with a fuel gas chamber and a filter upper end inner cavity, two ends of the air pipe are respectively connected with the right tee joint and the middle inner cavity of the filter are respectively connected with a smoke exhaust pipe and a fuel gas pipe on the upper and lower end of the filter, the bottom of the filter is provided with a drain pipe. The biomass gas furnace has wide applicability, the generated raw fuel gas into clean fuel gas by several times processing or filtering and providing to the user, is provided with energy-saving environment-friendly effect, and has popularization and application value.
NOVELTY - Preparing an adsorbent comprising Schwertmannite, comprises (1) providing a composition comprising Schwertmannite and water in an amount of 7.5-25 wt.%, and (2) compacting the composition to provide a compacted composition.    USE - The method is useful for preparing an adsorbent, which is useful for: removing sulfur, selenium, tellurium, phosphorus, arsenic, antimony, bismuth, lead and cesium and a transition metal including chromium, molybdenum, uranium, radium, nickel, ytterbium, vanadium, cadmium and mercury, lanthanide or actinide from a liquid to purify liquid; and purifying gas/biogas such as hydrogen sulfide or hydrogen cyanide (all claimed).    ADVANTAGE - The method easily and economically prepares the adsorbent with good filter stability and high abrasion resistance.    DETAILED DESCRIPTION - Preparing an adsorbent comprising Schwertmannite, comprises: either (1) providing a composition comprising Schwertmannite and water in an amount of 7.5-25 wt.%, and (2) compacting the composition to provide a compacted composition; or (1a) the step (1) as above per se, (2a) mixing the composition with an organic polymer or its precursor to provide a mixed composition, and (3a) solidifying or curing the organic polymer to provide a solidified or cured composition or compacting the mixed composition to provide a compacted composition. An INDEPENDENT CLAIM is included for use of Schwertmannite for the purification of biogas including hydrogen sulfide by first contacting Schwertmannite with a phosphate containing solution and then with the biogas.
NOVELTY - Optimizing the energy production in biogas plants, comprises measuring the filling level of the gas reservoir or buffer gas, passing to the control system, which controls the introduction of solid and/or liquid substances into the fermenter, and controlling or regulating the fermenter depending on the value of the introduction.    USE - The method is useful for optimizing the energy production in biogas plants.    ADVANTAGE - The method: ensures continuous gas production; and prevents over-production of biogas, thus it avoids unwanted emissions of methane.
NOVELTY - Producing biodegradable polymer and biomass fuel converted from carbon source by recombinant microorganisms, comprises: providing recombinant microorganisms transformed with plasmids containing at least a gene that encodes glycerol utilizing enzyme, and gene that encodes polyhydroxyalkanoate synthase; culturing the microorganisms in medium containing glycerol; inducing expression of genes to obtain polyhydroxyalkanoate and ethanol; and recovering polyhydroxyalkanoate and the ethanol. The recombinant microorganisms have accumulated polyhydroxyalkanoate to biomass content of at least 30 wt/wt.%.    USE - The method is useful for producing biodegradable polymer and biomass fuel.    ADVANTAGE - The method: utilizes the recombinant microorganisms, which have a glycerol utilization rate of more than 90 wt/wt.% (claimed), as compared to non-transformed wild-type microorganisms; utilizes the crude glycerol as carbon source, hence reduces the cost, and avoids the need for pH regulation; and is environmentally friendly, as compared to conventional methods.
NOVELTY - Aerosol device comprises a cosmetic composition comprising 0.1-15 wt.% of one or more water insoluble calcium salts, one or more fixing polymers, one or more 2-4C monoalcohols, and one or more propellants.    USE - The composition is useful for shaping the hair and/or holding the hairstyle (claimed).    ADVANTAGE - The composition allows re-establishment of the shape of the hairstyle even after it has been intentionally or unintentionally modified in the course of the day without additional application of the product thus providing good volume and texture to the hair.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for shaping the hair and/or holding the hairstyle comprising applying the cosmetic composition sprayed from the aerosol device to wet or dry hair, and rinsing out or leaving in after an optional leave-in time or optional drying.
NOVELTY - Manufacture of regenerated clay involves carrying out pretreatment by maintaining a lower alcohol and waste clay used in refinement of oils and fats in a mixed state, and carrying out regeneration process by admixing an acidic catalyst into the pretreated mixture of clay and lower alcohol, simultaneously extracting an oily component from the clay and performing esterification between the lower alcohol and at least one component chosen from free fatty acid and an oil and fat in the extracted oily components.    USE - Manufacture of regenerated clay used for manufacture of refined fats (all claimed), and used as biofuel.    ADVANTAGE - The method enables efficient and economical manufacture of regenerated clay with improved decolorizing function by environmentally-friendly and simple process. The thermal recycling of manufactured ester can be easily carried out.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of ester with acid value of 0-10 mg potassium hydroxide/g; and    (2) manufacture of refined fats, which involves decoloring fats and oils using the regenerated clay.
NOVELTY - The method involves separating feed mixture in methane wash column (1) fed by liquid methane stream (11) at top of methane wash column to produce a gas (12) enriched in hydrogen. Liquid stream (13) is treated to produce a mixture of carbon monoxide and methane (15), from the bottom of methane wash column. The mixture of carbon monoxide and methane is separated in a separation column (3) to produce a gas enriched in carbon monoxide (16) and liquid methane flow (4). Volume of liquid methane stream is varied to take account of varying demands for gas enriched in carbon monoxide and hydrogen.    USE - Method for cryogenic separation of feed mixture of carbon monoxide.    ADVANTAGE - As the volume of liquid methane stream is varied to take account of varying demands for gas enriched in carbon monoxide and hydrogen, the use of carbon monoxide storage tank can be avoided, and the variations in demand for hydrogen and carbon monoxide can be accommodated. The overall amount of liquid carbon monoxide in the process can be decreased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for cryogenic separation of feed mixture of carbon monoxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram illustrating the method for cryogenic separation of feed mixture of carbon monoxide.    Methane wash column (1)    Separation column (3)    Liquid methane flow (4)    Liquid methane stream (11)    Gas enriched in hydrogen (12)    Liquid stream (13)    Methane (15)    Carbon monoxide (16)
NOVELTY - A urea granulation process involves removing dust and ammonia using one or more gaseous waste stream contained in the scrubbing system, and processing the waste stream by generating dust-laden liquid stream and dust-reduced stream by washing the dust and ammonia laden stream (4) with water and/or aqueous urea solution, and forming a stream (8) comprising hexamethylenetetramine, urea formaldehyde and clean off-gas (6), by reacting the dust-reduced stream (5) with formaldehyde (7).    USE - Urea granulation process (claimed).    ADVANTAGE - The method provides fertilizer grade urea granules with reduced ammonium salt concentration, and is simple, economical and emits ammonia in reduced amount.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) scrubbing system, which is a complete closed system. The ammonium salt stream from the scrubber acid stage is fed into scrubber dust stage. The resulting solution from the scrubber dust stage is fed into an evaporation unit. The vapor stream containing ammonia is introduced into a condenser unit. The obtained liquid process condensate is fed into the scrubber acid stage. The concentrated liquor stream containing urea and ammonium salt is generated in the evaporation unit, and the obtained molten urea is conveyed into a urea granulator; and    (2) urea granulation apparatus. The apparatus consists of scrubber dust stage, in which the dust is washed off from the dust and ammonia laden stream, and formaldehyde stage, in which a portion of ammonia-laden air is reacted with formaldehyde, to form hexamethylenetetramine. The scrubber dust stage is arranged in the upstream of formaldehyde stage.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of urea granulation process.    Dust and ammonia laden stream (4)    Dust reduced stream (5)    Clean off-gas (6)    Formaldehyde (7)    Stream (8)
NOVELTY - The device has a device unit provided with a fractionating device and an air storage tank. A particulate filter is formed with an air outlet end and an air inlet end that are matched with a dehydrating device. The air outlet end is matched with a carbon dioxide removing device that is connected with the air inlet end. The air inlet end is fixed with a pipeline. The air outlet end is fixed with the fractionating device that is connected with the air storage tank. The air storage tank is connected with the air inlet end. The dehydration device is provided with a molecular sieve drying tower.    USE - Mobile coal bed liquefied methane purifying device.    ADVANTAGE - The device has high safety performance, and realizes low temperature high purity liquefying and separating processes, and separates the air outlet end so as to prepare liquefied natural gas and prevent air from polluting during discharging process. The device can effectively utilize a coal bed gas source. The device is fixed with a container, so that the device is convenient to move.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a mobile coal bed liquefied methane purifying device.
NOVELTY - This utility model claims a sewage treatment system, comprising a sewage pipe and the sewage pipe along the sewage flowing direction in turn set the mechanical grid, on-line monitoring sub-system and automatic medicine applying sub-system, on-line monitoring sub-system and automatic medicine applying sub-system are connected with a server by the wire or wireless mode, a on-line monitoring sub-system and the automatic medicine applying sub-system spacing distance of the first length, on-line monitoring sub-system for monitoring and transmitting the data to the server, the server control automatic medicine applying sub-system of each section of sewage is applied medicament is a dosage according to the monitoring result to the flow through each section of the sewage on-line monitoring sub-system. This utility model is characterized by low cost, simple building, the process time is short, the performance.
NOVELTY - This utility model claims a kind of used for rotating roller type aerobic fermentation treatment device of organic waste is inner environment control system for outdoor shell system. The system comprises a material temperature sensor and the oxygen concentration sensor material aerobic fermentation cylinder, and gas circulating system connected with the central control system is connected with the air outlet, wherein the temperature of the material of the material sensor and the oxygen concentration sensor in at least one group respectively extend into the interior of the rotary drum to the rotating drum-type aerobic fermentation treatment device of organic waste, and the output end of them are respectively connected to the central control system by a brush or a wireless communication, the control end of the central control system is connected with the control motor of the gas circulation system. Aerobic fermentation cylinder using the control system can accelerate speed of aerobic fermentation reaction, improving the working efficiency of the fermentation cylinder so as to realize full automatic control device, so the utility model will make great contribution for low carbon economy and environmental protection.
NOVELTY - This utility model claims a kind of organic waste aerobic fermentation treatment device. The device further comprises a gas inlet device, a tail gas discharge device and a temperature measuring oxygen control system on the traditional aerobic fermentation treatment device, the aerobic fermentation cylinder and end cover, and is provided with an air inlet on a separate connected into the interior of the rotary drum to the inlet device of the air inlet, the back end of cylinder is provided with a discharging port, the aerobic fermentation cylinder front end is provided with a tail gas discharge device, the tail gas exhaust device and the tail gas can pass through and a deodorization by discharging the ventilating pipe, air pump, and is connected with the device, at the same time, measuring temperature and oxygen control system is connected to the aerobic fermentation cylinder. The device not only solves the problem that the compost period longer, bonding material easily block the composting mass, generated percolate is nitrogen loss and secondary pollution, large free land, and can realize continuous automatic operation and so on, but also obviously reduces the energy consumption, reduces the cost of the compost.
NOVELTY - This utility model claims an organic solid waste aerobic compost device, comprising a feeding mixer, a conveyor, a fermentation tower, a scraper driving device, a blower, a heating device, an exhaust fan, a waste gas processing device, a central discharge tray, the periphery discharging tray, a rotating disc type granulator, drive device, returning conveyor, granulating agent adding device and a spiral conveyor, wherein the fermentation tower is provided with a sealing cover, the rotating machine is connected with the lower part of the fermentation tower, a feeding through feeding port of the conveyor and the sealing cover. The utility model is provided with treatment of organic solid waste to realize reduction, stabilization, harmlessness and resource, and small floor area, at the same time it has to carry out automatic feeding, pelleting, processing automatic control ventilation, temperature control, tail gas.
NOVELTY - This utility model claims a kind of bio-diesel esterification tower. The esterification tower is mainly composed of tower body, methanol emptying pipe, a pressure reducing valve, a temperature measuring point, measuring point, de-foaming baffle plate, a mixing chamber, a discharge port, a sampling port, inlet, outlet, a manhole, a feed pipe, a bubbling pipe, a slag-drip opening. Methanol is provided with emptying valve, a pressure reducing valve, a measuring point in the tower body, the top is provided with two layers of de-foaming baffle plate on the upper part of the tower body, a tower body a as material, and is filled with filler, the material outlet is set one side of the filler lower part de-foaming baffle plate upper part of the tower body is provided with a sampling opening, the lower part of the tower body is provided with inlet and outlet, one side of the lower part of the tower body is provided with a manhole and a feeding pipe, and the other side of the lower part of the tower body is provided with a bubbling pipe and temperature measuring point and the bottom of the tower is provided with a slag. The esterification tower can speed up the esterification, transesterification reaction speed, but also improves the bio-diesel.
NOVELTY - This utility model claims a water electrolysis hydrogen oxygen device, comprising: in the inner cavity of the inner shell is filled with electrolyte, which is equipped with immersion into the electrolyte of the hydrogen oxygen generator is sleeved on the inner shell, and the shell to form a radiating air with the inner shell between the air outlet, the hydrogen and oxygen out of the cavity of the shell top part out of the shell, and is connected with a hydrogen leading-out pipe, the positive and negative electrode wiring of the hydrogen oxygen generator is fixed on the sealing top cover of the oxy-hydrogen leading-out cavity, the air inlet and the air outlet of the shell are an inlet and an outlet of the radiating air duct, and a fan on the radiating air channel. This utility model claims a water electrolysis hydrogen oxygen device solves the problem that the current water electrolysis hydrogen oxygen device radiating efficiency is low in the electrolysis process, so there is no need to increase the volume of the whole device, and finally reduces the manufacturing cost of the device, low power consumption and the user using cost.
NOVELTY - A radiating structure of hydrogen-oxygen generating device, comprising a cell and a radiating unit, wherein a is a number of at least one electrode plate, a top is provided with connected with veil of the gas pipe and a heat sink unit and electrolytic bottle, the radiating unit is provided with a fin with a circulation flow passage, one end of the flow channel is connected with the bottom is provided with a cell of the guide pipe, the guide pipe is provided with a pump, the other end of the flow passage is provided with a reflowing pipe connected with a electrolytic top part and a heat sink unit has blower set at one side of the fin radiating structure of the hydrogen and oxygen generating device can fast and uniform to radiate, so as to not influence the electrolytic action by the high temperature so as to improve the electrolysis efficiency so as to reach the purpose of energy-saving, and it can reduce the damage to the environment.
NOVELTY - This utility model claims a kind of a harmful gas monitoring instrument is GSM short message alarming, comprising a microcontroller, a liquefied gas detecting module, a carbon monoxide detecting module, detecting module, an A/D converter, a display module, an alarm module, a telephone module, a GSM module, a SD card memory and a power supply module, a display module, an alarm module, a telephone module, a GSM module and an SD card memory is connected with the micro-controller is connected with the alarm module and telephone module, the gas detecting module, a carbon monoxide detecting module, detecting module is connected with the A/D converter and micro controller, wherein the power supply module is in charge of power supply to the system. This utility model through telephone and GSM network real time monitoring harmful gas concentration, makes full use of public switched telephone network and GSM network covering surface is wide, there is no distance limit, a stable performance, visibility is good, and it has application and popularization value.
NOVELTY - Pyrolysis reactor comprises a main body composed of an upper furnace plate, a distributing plate, a lower furnace plate, a scraping plate, and a furnace dust blocking plate, where the upper furnace plate, distributing plate, dust blocking plate and the scraping plate can rotate, and the lower furnace plate and the furnace wall are stationary.    USE - The pyrolysis reactor is used in pyrolysis of low metamorphic coal, oil shale, oil sands, biomass, waste tyre, plastic, and macromolecular organic solid material (claimed).    ADVANTAGE - The reactor utilizes distributing plate, which can realize the function of feeding or discharging through the rotation; is simple in structure; is provided with reliable operation; is convenient to maintain; and has large production capacity, and raw material suitability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the pyrolysis reactor.
NOVELTY - The system has an electrolytic water dismantling device that is coupled with a hydrogen combustion furnace of heat carrier cladding portion, based on fluidized beds. The fluidized bed in hydrogen combustion furnace contains sand, fluidized bed material, silicate (SiO3), quartz sand, mixed corundum, normal corundum and special fused alumina, oxides, hydroxide, aluminum compounds, silicates and other inorganic solids.    USE - System for operating water electrolysis device and hydrogen combustion furnace.    ADVANTAGE - By the transmission of heat combustion to heat carrier, the efficiency of hydrogen combustion furnace can be improved. Thus, carbon-free power generation can be ensured effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for operating water electrolysis device and hydrogen combustion furnace.    Lead burner (4)    Double-walled combustion chamber (6)    Flue gas outlet (7)    Steam outlet (8)    Control valve (10)
NOVELTY - The method involves executing a feed-forward control scheme to determine amount of post-combustion fuel to achieve preferred temperature in the exhaust gas feed-stream at an inlet to particulate filter (64). The amount of post-combustion fuel comprising nominal post-combustion fuel amount is adjusted for bio-diesel blend ratio of the fuel. The post-combustion fuel upstream of the exhaust after-treatment system (60) is injected in response to the command to regenerate the particulate filter.    USE - Method for operating compression-ignition engine coupled to exhaust after-treatment system including particulate filter, for use in engine-transmission system and hybrid powertrain system.    ADVANTAGE - Since the bio-diesel blend ratio is increased, the particulate matter loading on the particulate filter is decreased. Hence, the extended operation between regeneration events of the engine is ensured. The time lag is introduced in the transition from change in temperature from the inlet temperature of the oxidation catalyst to the blend ratio-corrected reference temperature, thus over-fueling of the post-combustion injection due to thermal lag associated with warm-up of the oxidation catalyst is prevented. The mass flow-rate of fuel with respect to the compression-ignition engine is achieved by controlling injector pulse-width that includes information about fuel pressure and volumetric flow-rates.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compression-ignition engine.    Compression-ignition engine (10)    Cylinder (20)    Exhaust gas sensor (40)    Exhaust after-treatment system (60)    Particulate filter (64)
NOVELTY - The system (1) has water electrolysis apparatus (30) that is provided for sending out hydrogen and oxygen containing water vapor. A drying apparatus (60) is provided with water electrolysis stacks (51-1,51-2) for supplying oxygen to anode side of electrolytic membrane and hydrogen to cathode side of electrolytic membrane, for removing water vapor from oxygen and hydrogen. A power supply unit (55) is provided for supplying voltage between anode and cathode of electrolytic membrane, and for sending electric current through water electrolysis stack.    USE - Water electrolysis system.    ADVANTAGE - The moisture content in the saturated vapor pressure included in oxygen and hydrogen which are obtained by water electrolysis can be removed effectively for supplying dry oxygen and hydrogen, by providing drying apparatus having water electrolysis stacks for supplying oxygen to anode side and hydrogen to cathode side of electrolytic membrane, for removing water vapor from oxygen and hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water electrolysis system. (Drawing includes non-English language text)    Water electrolysis system (1)    Water electrolysis apparatus (30)    Water electrolysis stack (51-1,51-2)    Power supply unit (55)    Drying apparatus (60)
NOVELTY - A hydrogen generating electrode groups, hydrogen generating machine further comprises a. the first electrolytic bath and the electrode group is set with said main shell, an electrode group comprises two installed on the main outer surface of the shell of the electric connector, the two are respectively connected with the power joint of the metal connecting unit, and a plurality of separated from each other is set in the electrolytic cell is set with a upper metal plate electrode connected to each of the electrode plate is a flat plate, and comprises two metal for connecting unit of the electrode hole, the first hole formed on the electrode of the main channel, adjacent the first edge to form a ring channel and multiple air outlet set on the electrolytic hole of main channel formed adjacent to the electrode plate of the annular channel, hole is opened on the main channel, which effectively avoids point discharge, and can improve the hydrogen production efficiency.
NOVELTY - A hydrogen generator comprises a main shell body, a cover body and at least one radiating unit, the main shell comprises a electrolytic tank, a cover body is covered on the main shell, the cover body comprises a water inlet pipe, wherein the radiating unit comprises one and mounted on the main shell and is set on the radiating tube of the electrolytic bath and two fixing holes which are used for connecting the radiator pipe on the metal gasket of the main shell, the metal gasket is located between the main outer surface of the shell, and the utility model is lifting the hydrogen passes through the radiating unit generates heat dissipation rate of a, and the radiating pipe is set in the electrolytic tank, the heat energy with the electrolytic bath to the metal gasket, the heat can be dissipated via the metal gasket on the main outer surface of the shell is made of metal.
NOVELTY - This utility model claims bean waste treatment device. And the step of processing waste water and device is composed of a waste water orderly flows through an adjusting pool, a hydrolysis acidification pool, an anaerobic pool, biological synchronous degradation tank and mud-water separating device. The hydrolysis acidification pool and macromolecule matter hydrolyzing into a soluble substance and degradation COD, anaerobic tank generating methane at the same time to degrade COD of biological synchronous degradation pool using a dissolved oxygen aeration synchronous degrade COD and N of biological synchronous degradation pool end mixed solution reflux to the water end, to a mud-water separating device, the mud-water separating the clean water discharged sludge reflux water inlet end of a hydrolysis acidification pool, the residual sludge is discharged sludge treatment system. This utility model beneficial effects: the whole biochemical treatment technology and synchronous degrade COD and N, the treated water reaches the integrated wastewater discharge standard (GB8978-1996) of the first level discharge standard, which solves bean product waste water processing N, large amount of sludge and the cost is high.
NOVELTY - This utility model belongs to biomass thermal conversion technology field, especially relates to a kind of multi-products of the carbonizing and activating, pyrolysis and gasification, catalytic cracking device. The device is composed of a smoke channel (1), gas agent inlet (2), an auxiliary active gas agent inlet (3), a feeding port (4), a feeding sealing device of gear cover (5), a blanking forced shovelling plate (6), a feeding cover (7) (8), a transmission and a gear box (9), a heat insulating cotton (10), a rotating ring (11), an angle adjusting bolt (12), a cylinder (13), a cylinder bracket (14), a temperature measuring device (15), a combustion passage (16), passage (17), an angle adjusting screw rod (18), a discharging sealing device of gear cover (19), a discharging cover (20), an ignition port (21), an explosion-proof opening (22), a combustion-supporting port (viewing port (23), a discharging seal valve (24), a discharge cooler (25). This utility model by changing the tilt angle, the rotating speed and a sealing method and at the same time both carbonizing and activating, pyrolysis gasification and catalytic cracking and so on. The traditional direct combustion method is changed into heat radiation method, solves the problem that the biomass thermal transition process has low yield from the process aspect, ignition, reaction and production, consumption and temperature is difficult to control and so on.
NOVELTY - The device has container which is provided with air inlet and air outlet. The air inlet is located under the liquid level of filter liquid. The air outlet is located on the liquid surface of filter liquid. The air outlet is connected with air inlet branch pipe (11). The hydrogen and oxygen gas is generated in tank (3). The positive and negative electrodes are connected with air inlet and automatic controller (4) respectively. The controller is provided for controlling the generated hydrogen and oxygen flow rate, and is connected with vehicle battery (5).    USE - Hydrogen-oxygen mixed power device for vehicle.    ADVANTAGE - The fuel oil can be saved efficiently. The environmental pollution can be prevented effectively. The hydrogen and oxygen gas purity can be ensured. The occurrence of hydrogen and oxygen annealing effect can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen-oxygen mixed power device.    Tank (3)    Controller (4)    Vehicle battery (5)    Ventilation hose (9)    Air inlet branch pipe (11)
NOVELTY - The briquette comprises a graphical user interface, a set of central penetration holes through which the air passes, and outer side surfaces formed with curved surfaces to form a curvature at a predetermined ratio. A holding portion is formed in a side of the briquette. A projection is formed in an inner side of the briquette, and is identical with the outer side surface. The corners of the cube are tapered. A nature igniter comprises an igniting composition that is formed by mixing alcohol and a binder including coconut husk, rice hulls, transfer, bamboo and mangrove.    USE - The briquette is useful for cooking meat e.g. beef or pork.    ADVANTAGE - The briquette prevents a grilling part from being easily broken when the user moves the briquette. The briquette is laminated, so that user can conveniently use the briquette. The user can easily ignite the briquette and prevents the generation of the contaminant.    DETAILED DESCRIPTION - The briquette comprises a graphical user interface, a set of central penetration holes through which the air passes, and outer side surfaces formed with curved surfaces to form a curvature at a predetermined ratio. A holding portion is formed in a side of the briquette. A projection is formed in an inner side of the briquette, and is identical with the outer side surface. The corners of the cube are tapered. A nature igniter comprises an igniting composition that is formed by mixing alcohol including methylalcohol, ethyl alcohol, propyl alcohol, isopropyl alcohol and butyl alcohol and a binder including coconut husk, rice hulls, transfer, bamboo and mangrove.
NOVELTY - A sorbent medium comprises at least one self-supporting porous body produced by sintering a mixture of a powdered adsorbent and polyethylene particles having a molecular weight of at least 4x 105 g/mol as determined by ASTM-D 4020.    USE - As sorbent medium for a cyclic adsorption process (claimed), or for separation of gases by cyclic adsorption processes, especially pressure swing adsorption. Also useful in a large variety of gaseous separations, including recovery of nitrogen from air, purification of hydrogen from synthesis gas, methane upgrading from biogas (e.g. landfill gas), ethane separation from methane (shale gas), and carbon dioxide removal from flue gas.    ADVANTAGE - The adsorbents are improved adsorbents for pressure swing adsorption (PSA) systems that will increase the availability and accessibility of active sites resulting in fast mass transfer kinetics and high working capacity and decrease the pressure drop to enable higher throughput without fluidization. A composite block or sheet produced by sintering a mixture of a powdered adsorbent and a high and/or ultra high and/or very high molecular weight polyethylene powder exhibits improved properties as a structured adsorbent for cyclic adsorption processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cyclic adsorption process for separating a first gas component from a feed gas mixture comprising at least a first gas component and a second gas component, involving: providing the sorbent medium; supplying the feed gas mixture to an adsorption zone containing the sorbent medium such that the second gas component is preferentially adsorbed by the sorbent medium; and recovering the first gas component from the adsorption zone.
NOVELTY - Converting biomass into a digestible animal feed, comprises comminuting biomass into smaller fractions, and contacting the smaller fractions with a hydrolyzing agent and water at a moisture content of 25-55% at ambient temperature and ambient pressure to produce a treated biomass.    USE - The method is useful for converting biomass such as corn stover into a digestible animal feed (all claimed).    ADVANTAGE - The continuous method allows economical conversion of biomass into a more digestible animal feed with reduced energy consumption and high yield in a consistent manner.    DETAILED DESCRIPTION - An INDEPENDENT claim is included for a system for converting biomass into a digestible animal feed, comprising a device for comminuting biomass into smaller fractions, a conveyer (20) for moving the smaller fractions from the device, and units for spraying an aqueous solution comprising an inorganic hydrolyzing agent onto the smaller fractions on the conveyer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a system for converting biomass into a more digestible animal feed.    Container (10)    Hose (12)    Pump (14)    U-shaped manifold (18)    Conveyer. (20)
NOVELTY - Method of combating or controlling insects of Diabrotica genus on crop plants, involves applying novaluron on the crop plants when the targeted Diabrotica insects reach adulthood.    USE - The method is useful for combating or controlling insects of Diabrotica genus chosen from D.virgifera, D.barberi, D.balteata, D.beniensis, D.cristata, D.curvipustulata, D.dissimilis, D.elegantula, D.emorsitans, D.graminea, D.hispanolae, D.lemniscata, D.linsleyi, D.longicornis, D.milleri, D.nummularis, D.occlusa, D.porracea, D.scutellata, D.speciosa, D.tibialis, D.trifasciata, D.undecimpunctata, and D.viridula, preferably D.virgifera, D.barberi, and D.undecimpunctata, in crop plants chosen from maize, cotton, and soybean (all claimed).    ADVANTAGE - The method is environmentally-friendly, reduces risk of residues and intoxication, exhibits rapid effect even in low dosage, enables to improve yield of crops, and prevents egg hatching of insects.
NOVELTY - Method for cooling material flow (S) involves introducing material flow (S') into encased chamber of a device of olefin system in which the chamber is delimited by a casing, arranging a plate heat exchanger in the encased chamber such that material flow (S') in the encased chamber forms a bath which surrounds the plate heat exchanger, introducing to-be-cooled material flow (S) into the plate heat exchanger in countercurrent to material flow (S'), and exchanging heat indirectly with the material flow (S') such that material flow (S) is condensed and material flow (S) is evaporated.    USE - Method for cooling material flow (claimed).    DESCRIPTION OF DRAWING(S) - 123456: NO DESCRIPTION REQUIRED
NOVELTY - Manufacture of biodiesel involves producing pellets by centrifugation, adding alkyl alcohol, performing transesterification reaction in presence of microorganism, and extracting fatty acid methyl ester from the resultant reaction mixture.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel with high yield, by a simple process. The biodiesel is environmentally-friendly.
NOVELTY - The tank has a cylinder hydrogen separation tank that includes two holders and stores electrolyte solution. A stainless steel lid (2) is welded onto tank. The top of lid is provided with holes to install anode shaft (5), cathode shaft (6), neutral shaft and thermometer (4), electrolyte solution refilling pipe (8), and hydrogen pipe connector (3). A permanent magnet (12) is covered in stainless steel case, and positioned in between cell plates (11) and connected to anode. A stainless steel plate (13) is attached to the anode shaft holding the cell plates and the permanent magnet.    USE - WDH7 hydrogen separation tank.    ADVANTAGE - Since the stirrer set is attached to the anode shaft holding the cell plates and the permanent magnet, the flow speed of electrolyte solution is increased and the reaction to produce hydrogen gas is increased, when electrical current is passed through the electrolyte solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the WDH7 hydrogen separation tank and tank lid.    Stainless steel lid (2)    Hydrogen pipe connector (3)    Neutral shaft and thermometer (4)    Anode shaft (5)    Cathode shaft (6)    Electrolyte solution refilling pipe (8)    Cell plates (11)    Permanent magnet (12)    Stainless steel plate (13)
NOVELTY - A kind of efficient, integrated and the energy-saving, decomposition in the integrated kitchen waste processing device. A kind of spiral extrusion with function of solid-liquid separation device, comprising a feeding hopper, a material conveying device, a material pressing device, a speed reducing motor, a mechanical extrusion dehydration of garbage, the spiral extruding functions of solid-liquid separation device with stirring, heating, fermentation device of the garbage organic aeration function are integrated, the floor area is small, which saves energy and is convenient for operation control, full closed design, there is no exposed, it has no pollution to the environment to be treated garbage material a course of treatment.
NOVELTY - The utility model claims a multifunctional earthworm biological organic garbage processor, belonging to the technical field of garbage processor. Is provided with a filling port (machine body (1), a machine body (1) of the left and right two ends of the shaft of the motor (5) is connected with a machine body (1) from the ground (2), the side wall of the machine body (1) is provided with an opening, the opening from the inside to the outside and the machine body (1) is provided with a mesh screen (3), a detachable sealed clapboard (4), a machine body (1) is further equipped with a ventilating natural ventilation system. This utility model has reasonable structure design, simple operation, can make household garbage changes waste into valuable.
NOVELTY - This utility model claims a test compost gas-generating amount of the dynamic type composting device, comprising a box body, a rotating shaft, a stirring paddle, a oxygen probe, a temperature probe, a motor, a speed reducer, a first flow meter, an air pump, a pipe, storage bag and a flow meter, wherein the box body is provided an air inlet and an air outlet, the box body is equipped with a rotating shaft, the rotating shaft is set with a stirring paddle, an oxygen probe and a temperature probe is installed in the box body, the rotating shaft is connected with the speed reducer, the speed reducer is connected with the motor, the air outlet through the first flow meter is connected with an air pump, an air pump and connected with pipe, pipe passes through the second flow meter and the gas storage bag is connected is connected with the exhaust pipe. This utility model overcomes the problem that the gas accumulated in the tank, one can measure a period of time the gas discharge rate and can accurately measure a day generating amount and so on, it has simple structure and low cost, the gas update frequency in real time measuring balance conditions of gas discharge rate and accurately measure gas generating amount and so on.
NOVELTY - This utility model claims a hydrogen preparing system, comprising a main control system, a storage unit, a wind power unit, a processing unit and a producing unit, a main control system by control cable are respectively connected with the electric power storage unit, a wind power unit, a processing unit and a hydrogen production unit, electric power storage unit comprises a battery electric power storage device and electric control module, according to the wind power unit comprises a wind generating machine set device and electronic control module, a processing unit comprises a processing device and a processing control module, a producing unit comprises an electrolytic hydrogen producing device and hydrogen production sub-control module. This utility model use the earth's surface of the reproducible wind energy, converting it into supply electrolytic hydrogen producing device for generating electricity via wind power generator device, wherein battery electric power storage device storage system automatically controlling continuity problem of water electrolysis hydrogen production system of the pure water supply by a processing device, finally providing high purity hydrogen output for the terminal user. This utility model provides a set of environment protection and energy saving system of decomposing ammonia to produce hydrogen.
NOVELTY - A kind of convenient to use a hydrogen generator, comprising a hydrogen reactor and a controller, hydrogen reactor in plug connection with the controller, mouth pull plug is set in the normally closed valve plug, the hydrogen reactor is inserted into a control valve is opened, the hydrogen and the assembly controller is connected with the hydrogen of the hydrogen on the controller. Hydrogen reactor when the reaction ending, to exchange new continue taking hydrogen, it is convenient for a long time.
NOVELTY - This utility model claims an excrement processing device, comprising: a receiving device for receiving, receiving device is provided with a feeding port, a discharging port and a plurality of steam inlet, a steam supply device, is connected with the steam inlet and steam to provide heat for a receiving device, the receiving device of the excrement; storage device which is connected with the discharge hole, which is used for storing and cooling, conveying device, which is used for containing the device to the memory device by the waste heat and the waste after heating. The utility model use the excrement treatment device, the excrement by heating and curing in the transmission process by the heating device so as to reach the effect of the excrement fermentation so as to reduce the processing time of the excrement.
NOVELTY - The utility model claims a kind of fertilizer for producing device, specifically to a crop micro fertilizer seed culture tank, comprising a tank body, a supporting rod is supported on the lower part of the tank body and a motor on the outer side of the upper and lower ends of the tank body is provided with a feeding pipe and a discharging pipe, the tank body is provided with a vertical stirring shaft, the upper end of the stirring shaft extends to the output shaft of the tank body outer side is connected with the motor, wherein the lower end of the discharging pipe is provided with a detachable sealing cover is connected to the discharging pipe, because it adopts the said structure, the utility model is a biologic bacterial manure for large-field crops seed culture tank is provided with more than one reaction space, the strain more efficient and improves the quality of the fertilizer, and the reaction is more thoroughly.
NOVELTY - A kind of biological diesel oil pre-processing deacidifying device, mainly composed of methanol overhead tank (1), oil tank (2), a flow meter (3), reaction column (5), overhead tank (1), oil tank (2) are respectively connected with the flow meter (3) and a reaction column (5), wherein the SK is provided with a static mixer and the flow meter (3) and the reaction column (5) (4) is a reaction column, a static mixer (4) (5) is connected with the inlet, is further provided with a ((/yanlu:)) groove at the back of the reaction column (5) (6). The beneficial effect of the utility model is, it can make the raw material for preparing biological diesel oil continuously, and in the process of de-acidifying water continuous, so as to prepare the biological diesel oil ester exchange reaction of raw material for continuous supply, improve the yield of biodiesel.
NOVELTY - This utility model claims a biological pre-processing a deacidifying device, mainly composed of methanol overhead tank (1), oil tank (2), a flow meter (3), reaction column (5), overhead tank (1), oil tank (2) are respectively connected with the flow meter (3) and a reaction column (5), wherein a mixing tank and the flow meter (3) and a reaction column (5) (4) is a reaction column, a mixing tank (4) (5) is connected with the inlet, is further provided with a ((/yanlu:)) groove at the back of the reaction column (5) (6). The beneficial effect of the utility model is, it can make the raw material for preparing biological diesel oil continuously, and in the process of de-acidifying water continuous, so as to prepare the biological diesel oil ester exchange reaction of raw material for continuous supply, improve the yield of biodiesel.
NOVELTY - This utility model claims a biological pre-processing a continuous deacidifying device, mainly composed of a methanol tank, oil tank, sulphuric acid high-level tank, a high-level tank, a flow meter, a reaction kettle, methanol tank, oil tank respectively by the flow meter from the same pipe and the reaction kettle connected, sulphuric acid high-level tank by the flow meter and the reaction kettle is directly connected with pipeline, wherein the reaction kettle and an oil-water separation tank and is provided with a SK static mixer, the static mixer inlet and the reaction kettle upper part outlet connected with the oil-water separating groove to the back thereof is further provided with a filter groove. According to the high position water tank, connected with a flow meter and the outlet pipeline of the reaction kettle. The beneficial effect of the utility model is, it can make the raw material for preparing biological diesel oil continuously, and in the process of de-acidifying water continuous, so as to prepare the biological diesel oil ester exchange reaction of raw material for continuous supply, improve the yield of biodiesel.
NOVELTY - This utility model claims a new biological pre-processing deacidifying device, mainly composed of a methanol tank, oil tank, sulphuric acid high-level tank, a high-level tank, a flow meter, a reaction kettle, methanol tank, oil tank respectively by the flow meter from the same pipe and the reaction kettle connected, sulphuric acid high-level tank by the flow meter and the reaction kettle is directly connected with pipeline, wherein it further comprises a mixing tank, the inlet on the side of the middle part of the reaction kettle and the outlet pipe, and the outlet of the mixing tank and the side of the oil-water separating groove connected with the oil-water separating groove is with a salt filter groove. According to the high position water tank, connected with a flow meter and the outlet pipeline of the reaction kettle. The beneficial effect of the utility model is, it can make the raw material for preparing biological diesel oil continuously, and in the process of de-acidifying water continuous, so as to prepare the biological diesel oil ester exchange reaction of raw material for continuous supply, improve the yield of biodiesel.
NOVELTY - A biodiesel preparing esterification reaction tower comprises a tower body whose bottom part is provided with a gas phase methanol inlet, a discharge hole, a water outlet, a heat conducting oil jacket, a heat conducting oil inlet and a heat conducting oil outlet. A top part of the tower body is provided with a divider. An inner wall of the tower body is uniformly distributed with multiple baffle plates. The tower body is provided with a feeding port, a water inlet, a safety valve, a thermometer, a pressure gauge and a gas phase methanol outlet.    USE - Esterification reaction tower for preparing biodiesel.    ADVANTAGE - The tower has low reaction pressure and reaction temperature, less investment and operating cost and high yield, and consumes less energy and avoids utilizing catalyst and polluting environment.    DETAILED DESCRIPTION - A biodiesel preparing esterification reaction tower comprises a tower body whose bottom part is provided with a gas phase methanol inlet, a discharge hole, a water outlet, a heat conducting oil jacket, a heat conducting oil inlet and a heat conducting oil outlet, where the tower body is provided with a distributor that is connected with the gas phase methanol inlet. A top part of the tower body is provided with a divider. An inner wall of the tower body is uniformly distributed with multiple baffle plates. The tower body is provided with a feeding port, a water inlet, a safety valve, a thermometer, a pressure gauge and a gas phase methanol outlet.
NOVELTY - The system has a coupling element (2) for attachment of a tubing (1) to an aperture (4) formed in a wall (5) i.e. pane, of a housing. The coupling element has an insulation portion (7) insertable through the aperture to enable a connection with the wall, where the insulation portion is made of material such as plastic, exhibiting thermal conductivity less than 5 W/mK. The insulation portion partially encloses a heating device (6) to define a low thermal conductive region between the heating device and the wall, so that thermal decoupling of the heating device from the wall is enabled.    USE - Tubing system for transportation of reaction water produced in a fuel cell system of a motor car.    ADVANTAGE - The insulation portion partially encloses the heating device to define the low thermal conductive region between the heating device and the wall, so that thermal decoupling of the heating device from the wall is ensured, and an unobstructed flow of heat energy into the wall is prevented, thus transferring large proportion of heat energy from the heating device into the tubing interior, and hence ensuring quick defrosting of a passage area in the region of the coupling element without using special additional heating systems even at very low ambient temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a tubing system.    Tubing (1)    Coupling element (2)    Aperture (4)    Wall (5)    Heating device (6)    Insulation portion (7)
NOVELTY - A zeolite film complex comprises zeolite film which is formed on inorganic porous support body and contains chabazite (CHA)-type aluminosilicate zeolite. Mole ratio of monovalent metal with respect to aluminum (Al) on surface of zeolite film is greater than or equal to 0.3. Zeolite film complex can permeate gas component with high permeability and can separate it from gaseous mixture containing gas components.    USE - A zeolite film complex for isolating or concentrating gas component from gaseous mixture containing gas components (claimed) used in chemical plant, fermentation plant, precision electronic components factory, and battery manufacturing factory.    ADVANTAGE - The zeolite film complex exhibits excellent chemical resistance, thermal stability, oxidation resistance, and pressure resistance and effectively separates gas component from gaseous mixture at low cost. Isolation method uses small-scale installation and is energy saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of isolating or concentrating gas component which involves contacting gaseous mixture with gas components and zeolite film complex and concentrating gas component with low permeability by permeating gas component with high permeability and separating from gaseous mixture or permeating gas component with high permeability and isolating.
NOVELTY - A zeolite film complex has a zeolite film comprising molar ratio of silica and alumina of 10 or less formed on a surface of a zeolite film containing aluminosilicate CHA-type zeolite which is formed on an inorganic porous support. The zeolite film complex is used to permeate component with high permeability and to separate from gaseous mixture.    USE - Zeolite film complex is used for separation or concentration of gaseous mixture of carbon dioxide, hydrogen, oxygen, nitrogen, methane, ethane, ethylene, propane, propylene, normal butane, isobutane, 1-butene, 2-butene, isobutene, sulfur hexafluoride, helium, carbon monoxide, nitrogen monoxide and water (all claimed).    ADVANTAGE - The zeolite film complex has excellent water resistance, chemical resistance, heat-resistant stability, oxidation resistance, voltage resistance and separation characteristics of gaseous mixture, and high wet heat stability. The gas with high purity is efficiently and economically separated from gaseous mixture with small-scale installation and reduced energy consumption, using the zeolite film complex.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separation or concentration method of gaseous mixture.
NOVELTY - A detonator type modifier (1) comprises cylindrical inner side pipe (10) which is provided in the inward of cylindrical inside pipe (20), inner side fin (11) which is provided in internal peripheral surface of inside by pass and protrudes from internal peripheral surface of inside by pass, inner side pipe inner space which is enclosed with internal peripheral surface of inside by pass, and reaction space (201) which is formed between internal peripheral surface of inside pipe and outer peripheral surface of inside by pass and in which catalyst is arranged and fuel and vapor circulate.    USE - Detonator type modifier for producing hydrogen used for high-temperature-form fuel cell.    ADVANTAGE - The modifier can heat the catalyst more uniformly using the circulated hot waste gas.    DETAILED DESCRIPTION - A detonator type modifier (1) comprises cylindrical inner side pipe (10) which is provided in the inward of cylindrical inside pipe (20), inner side fin (11) which is provided in internal peripheral surface of inside by pass and protrudes from internal peripheral surface of inside by pass, inner side pipe inner space which is enclosed with internal peripheral surface of inside by pass, and reaction space (201) which is formed between internal peripheral surface of inside pipe and outer peripheral surface of inside by pass and in which catalyst is arranged and fuel and vapor circulate. Under high temperature, the fuel and vapor react on catalyst in reaction space, and hydrogen is produced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional perspective view of the modifier of detonator type.    Modifier (1)    Inner side pipe (10)    Inner side fin (11)    Inside pipe (20)    Reaction space (201)
NOVELTY - A gas-generating system has water electrolysis apparatus (1) which electrolyzes water and produces gaseous hydrogen and gaseous oxygen, and oxygen expansion-cooling device (25,25a) which carries out swelling pressure reduction and lowers the produced gaseous oxygen in temperature.    USE - Gas-generating system is used for manufacture of hydrogen and oxygen.    ADVANTAGE - The gas-generating system has simple structure. The hydrogen and oxygen obtained by the gas-generating system have high purity and low humidity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation of gas-generating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a structure of the gas-generating system. (Drawing includes non-English language text)    Water electrolysis apparatus (1)    Oxygen gas-liquid separation portion (2)    Hydrogen gas-liquid separation portion (3)    Oxygen gas-liquid separator (22)    Oxygen expansion-cooling device (25,25a)
NOVELTY - A kind of sodium borohydride hydrolysis hydrogen fuel battery, comprising a liquid storage tank, a pump, a reaction tank, a purifier and a cold heat exchanger, in the liquid storage tank to store with a concentration according to weight ratio for NaBO4 15~30% solution of the liquid storage tank is fixed with a cold heat exchanger, pump through pipeline pump (NaBO4) solution to the reaction tank, a cold-heat exchanger into the reaction tank, the reaction tank is provided with catalytic agent support, adding reagent, a catalyst is provided with catalytic agent support, the catalyst support is fixed on the stainless steel wire gauze, reaction tank, reaction tank and the cold and hot exchanger steam pipe is connected, the air outlet pipe of the cold-heat exchanger arranged air outlet of the purifier, the purifier is arranged for a hydrogen fuel cell. Hydrogen produced is high purity, system high specific energy, good safety performance and long service life, the catalyst can be used repeatedly.
NOVELTY - A biodiesel manufacturing method involves selecting raw material oil, removing impurity, and performing dehydration process. The raw material oil is heated in a reaction tower. Lipid hydrolysis is performed with methanol gas and fatty acid esterification. Superfluous methanol gas is discharged, and the methanol is recycled. The reaction product is discharged from the tower. Crude glycerine and light component are removed. The fatty acid methyl ester is acidified. The obtained product is pumped into a fatty acid methyl ester distillation tower, and recycled.    USE - Method for manufacturing biodiesel without catalyst.    ADVANTAGE - The method enables manufacturing biodiesel with stable and reliable quality, in simple and cost-effective manner.    DETAILED DESCRIPTION - A biodiesel manufacturing method involves selecting raw material oil, removing impurity, and performing vacuum flash dehydration process. The raw material oil is heated in a reaction tower at 180-220 degrees C. Lipid hydrolysis is performed with methanol gas, grease, fatty acid esterification and glyceride ester exchange reaction for generating fatty acid methyl ester and glycerin. Superfluous methanol gas is discharged from the reaction tower, and the methanol is recycled in a methanol recovery tower. The esterification is separated from the methanol recovery tower, and the reaction product is discharged from the reaction tower. Crude glycerine and light component are removed, and temperature controlled to 160-185 degrees C. The fatty acid methyl ester is acidified. The obtained product is pumped into a fatty acid methyl ester distillation tower, and the temperature is controlled to 175-200 degrees C. The product is recycled at 180-240 degrees C to obtain fine methyl ester distillate, where the reaction product is mixture of methyl and crude glycerine, purity of methanol is greater than or equal to 98%, and the water content is greater than or equal to 0.1%.
NOVELTY - The utility model claims a kind of vegetable waste comprehensive treatment device, comprising a feed part and a bio-carbon part, a feed part comprises a first magnetic separator (1), a winnowing machine (2), the first drying machine (3), crusher (4), a stirrer (5) and a granulator (6), a feeding and conveying a feeding conveyor of biological carbon producing part comprises a second separator (7), a winnowing machine (8), the second dryer (9), retort (10), a gas-liquid separator (11) and a flue gas purifier (12), a feeding and conveying a feeding conveyor, solves the problem that the vegetable and straw wastes too much, the problem of polluting the environment.
NOVELTY - Preparing organic fertilizer comprises mixing high-efficient composite biological probiotics with wheat bran, corn powder or straw powder in a weight ratio of 1-3:100, mixing probiotics and livestock breeding waste material in a ratio of 1-10:100, fermenting in yeast fermentation medium at 60-75 degrees C in aerobic state, evaporating water to obtain the product, drying, and packaging.    USE - Used as a fertilizer.    ADVANTAGE - The fertilizer is prepared in a simple manner without pollution, and avoids peculiar smell, kills harmful bacteria during fermentation to ensure safe product, and ensures high utilization rate.
NOVELTY - A kind of preparing desert greening special fertilizer device, belongs to the field of agricultural machinery. The purpose of this utility model is for desert greening special fertilizer device a brown coal nitrogen low temperature plasma. The shaft of the motor is connected with the utility model is set with the reverse storage bin, the spiral pushing reactor, spiral propeller reactor, the feeding port is set with a rotary feeder on storage bin, the outlet of the reverse storage bin is set with a rotation type, nitrogen plasma generator is connected with the connected with the reverse. This utility model use plasma seed processing technology, seed treatment biological agent and chemical preparation for cost is lower than, and does not produce any pollution to the environment, increasing effect is obvious. Research has indicated, plasma treatment and corn 7%~10%, soybean 10%~15%, rice 8% to 10%, 10% to 15%, 10% to 30%.
NOVELTY - This utility model claims a kind of drier for fan and water storage device, belonging to the field of organic fertilizer production equipment technology field. The device comprises a water tank (5), an air inlet (3), a gas inlet (7), an air outlet (6) and a fan (2), fan (2) through the air inlet (7) is connected with the drying device (1), a fan (2) through the air inlet (3) is connected with the water tank (5) in water (4), an air outlet (6) communicates with the atmosphere. This utility model claims a kind of drier for fan and water storage device, reduces the environment pollution and improves the workshop production environment, it changes waste into valuable.
NOVELTY - The utility model claims a kind of using resources sewage treatment device of automatic flow reactor, comprising a grid, an adjusting pool, a pre-reaction tank, automatic reflux reactor, quick filtering tank, a disinfection device, a sludge concentrating tank, a sludge depth treatment device, a filter press, a sludge making fertilizer furnace, the reaction pool can be a aeration zone is hydrolysis acidification reaction pool or anaerobic reaction tank, the automatic return reactor, two inclined settling zone, an automatic return section, wherein said sterilizing device comprises a chlorine dioxide generator, an ultraviolet sterilizing device, wherein the sludge making fertilizer comprising a culture device, at, a reaction furnace, each device is connected with the pipeline, the utility model is new sewage treatment technology of the traditional active sludge method process of a return-flow system, and the sludge crushing and preparing fertilizer to replace the transporting the sludge cake, and is added with a quick filtering pool depth treatment and ultraviolet and a sterilizing of chlorine, it is provided with the good water quality, low energy consumption, small floor area, high-concentration active mud, strong impact resistance.
NOVELTY - This utility model claims composite kitchen garbage processor, comprising a processing box, a main motor and a rotating shaft, processing box comprises a first processing chamber and the second processing chamber, the first process chamber and the second process chamber is provided with a clapboard, the clapboard is provided with an overflow port, the overflow port is located on the rotating shaft, an overflow port is provided with a sealed overflow opening of the lift door, the rotating shaft passes through the first processing chamber and the second processing chamber, the main motor is connected with the rotating shaft, the rotating shaft is provided with a stirring arm, the bottom of the first processing chamber is provided with a discharge port at the bottom of the second processing chamber is provided with a discharge port, and a sieve plate, the sieve plate at the bottom of the second processing chamber is provided with a sewage tank, the upper part close to the side wall of the processing box is set at the bottom of the sewage tank is provided with a sewage outlet of the sewage tank. The utility model processing amount is large when the garbage can and garbage to ensure reduction treatment and garbage reduction fermentation for preparing organic fertilizer raw material are carried out at the same time.
NOVELTY - The utility model claims a new-type earthworm processing garbage biological organic fertilizer scattering device, comprising an outer shell, the outer shell is provided with a feeding hopper, wherein the first end is provided with an inclined sliding plate, a right middle part of the lower end of the hopper, the inner and outer shell body bottom part is fixedly provided with a symmetrical support frame, the upper support frame is provided with a track wheel, a roller wheel, a crawler track and is connected with a roller wheel, the track wheel by a transmission belt and the outer bottom of the shell is set with a motor, the bracket is further provided with a feeding hopper is installed on the upper part of the packing auger is connected, the first end is provided with a water tank. This utility model has simple structure, reasonable design, reduces pollution and earthworm by adequately disposing of the product falls into the hopper because of movement of the track bed, which is a biological organic fertilizer, composed of other mechanical or artificial method, package capable of selling, the bio-organic fertilizer.
NOVELTY - The method involves sealing and fixing an inner cylinder (5) on an oxide glass. A central electrode (1) is arranged at the inner cylinder. One end of an inserted sleeve (6) is contacted with the first pin electrode of the coaxial sleeve structure reactor case made of insulating medium. A ground wire (9) is extended from the cylinder. A circulation liquid inlet (7) is arranged at lower end of outer cylinder. A raw material gas inlet (8) is arranged at the lower end of the outer cylinder.    USE - Method for decomposing hydrogen sulfide, to prepare hydrogen used in chemical industries of natural gas, petroleum and coal.    ADVANTAGE - Since the grounding electrode is formed by temperature controllable circulating liquid, the decomposed sulfur can be separated through temperature control unit, so that continuous and stable operation of preparing the hydrogen through the decomposition of the hydrogen sulfide is ensured. The hydrogen and elemental sulfur can be prepared by dissociating the gases containing the hydrogen sulfide in chemical industries of natural gas, petroleum and coal. The special requirement for using source and the composition of the gases can be reduced so as to improve the universal applicability for preparing the hydrogen and the elemental sulfur through the decomposition of the hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating the process for decomposing hydrogen sulfide.    Central electrode (1)    Inner cylinder (5)    Inserted sleeve (6)    Circulation liquid inlet (7)    Raw material gas inlet (8)    Ground wire (9)
NOVELTY - The method involves sealing and fixing an inner cylinder (5) on an oxide glass. A central electrode (1) is arranged at the inner cylinder. One end of an inserted sleeve (6) is contacted with the first pin electrode. A platinum ground wire (9) is extended from the cylinder. A circulation liquid inlet (7) is arranged at lower end of outer cylinder. A raw material gas inlet (8) is arranged at the lower end of the outer cylinder.    USE - Method for continuously and steadily decomposing hydrogen sulfide gas to prepare hydrogen, used in natural gas industry, petroleum industry and coal chemical industry.    ADVANTAGE - Since the hydrogen sulfide or hydrogen sulfide-containing gas is subjected to axially reverse rotary flow through a dielectric barrier discharge area by adopting a spiral mode, the hydrogen sulfide can be decomposed by high-energy electrons in the discharge area, and the sulfur generated from decomposition can be centrifugally separated in time. The high-energy-efficiency decomposition of the hydrogen sulfide can be realized under the atmospheric and non-catalytic conditions. The hydrogen and sulfur produced from decomposition can be removed away from the discharge area in time, so as to stably perform the reaction operation of the hydrogen sulfide. The decomposition rate and the energy utilization rate of the hydrogen sulfide can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating the process for continuously and steadily decomposing hydrogen sulfide to prepare hydrogen.    Central electrode (1)    Inner cylinder (5)    Inserted sleeve (6)    Circulation liquid inlet (7)    Raw material gas inlet (8)    Ground wire (9)
NOVELTY - The portable hydrogen generator has an airtight container tank (1) that stores a hydrogen production mixture (4) and a liquid (3) respectively. An interconnected valve control pipeline (5), valve control liquid supplement and hydrogen discharge channel are arranged in generator main portion. An air pocket and a mechanical stirring device are arranged below the airtight container tank for storing the hydrogen production mixture, and are driven by virtue of an air pressure change in the airtight container tank.    USE - Portable hydrogen generator.    ADVANTAGE - The hydrogen production speed and safety of the hydrogen generator can be improved. Since the air pocket and mechanical stirring device are driven by virtue of air pressure change in the airtight container for storing the hydrogen production mixture, the product agglomeration in the reaction for hydrogen production can be eliminated effectively. The components used in hydrogen generator can be protected effectively. As the structure of the hydrogen generator is simplified, the size of the hydrogen generator can be minimized. The transporting effect and usability of the hydrogen generator can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the portable hydrogen generator.    Airtight container tank (1)    Liquid (3)    Hydrogen production mixture (4)    Interconnected valve control pipeline (5)    Closed air bag (9)
NOVELTY - A residual sludge methane yield improving method involves adjusting pH of sludge to be alkaline, followed by mixing uniformly, and standing for depositing. The supernatant is taken, and fed to an anaerobic expansion layer reactor to produce methane.    USE - Method for improving residual sludge methane yield of sewage treatment plant.    ADVANTAGE - The method enables recovering residual sludge in organic matter, and reducing the sludge to the environment.
NOVELTY - This utility model claims a kind of heat by biphenyl of diphenylamine reaction device, comprising a biphenyl heat-conducting oil boiler, the biphenyl heat-conducting oil boiler is connected with a biphenyl heater by pipeline, the biphenyl heater are respectively connected with a reactor product and the raw material heat exchanger, wherein the raw product heat exchanger is connected with a flash tank, the tank is further connected with a flash evaporation condenser, the biphenyl heat-conducting oil boiler is connected with water film dust remover through the pipeline. This utility model compared with single heating operation cost is greatly reduced, the safety factor is high, it saves energy, improves the enterprise benefit.
NOVELTY - Composting appliance comprises: at least a first container capable of containing compostable materials; a first temperature sensor configured to sense the temperature of either the first container or the compostable materials contained in the first container; a heating element in thermal communication with first container configured to heat first container to multiple temperature points; and a programmable controller in electrical communication with temperature sensor and heating element. The programmable controlled is programmed to heat the container at first and second temperature points.    USE - Used as composting appliance.    ADVANTAGE - The composting appliance: provides more efficient use of heat emitted from heating elements, potentially from a manufacturing and/or energy consumption perspectives; and can be able to carry simply to a desired location (e.g. flower bed) and tip over to release the compost without soiling the user's hands.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) composting comprising containing compostable material in a first container, heating the compostable materials contained in the first container to a first temperature, heating the compostable materials contained in the first container to a second temperature and composting the compostable material contained in the first container to compost; and    (2) a kit comprising the composting appliance and a unit dose article comprising a composting bacterium configured to be dosed into the composting appliance.
NOVELTY - Method for treating biomass, involves (a) pre-treating wet biomass, (b) extracting the pre-treated biomass with liquid water at a temperature between ambient temperature and 160 degrees C, (c) mechanically dewatering the extracted biomass to produce a dewatered biomass and aqueous effluent, (d) optionally heating the dewatered biomass at 160 degrees C or more, (e) drying the dewatered biomass, (f) optionally compacting the dried biomass to produce a solid material, and (g) subjecting aqueous effluent to anaerobic treatment.    USE - The method is useful for treating biomass, preferably fibrous biomass of woody plants, herbaceous plants, agricultural residues and forestry residues, is useful as fuel, preferably solid biomass-derived fuel, and producing biogas, electrical power and bio-alcohols, where the biomass comprises grasses, reeds and/or leaves (all claimed).    ADVANTAGE - The method dewaters and process biomass with relatively high water contents, ferments (anaerobically) aqueous fraction of wet biomass to a high degree, converts dewatered biomass to a useful solid fuel substitute having a high caloric value, discharges or reuses any residual effluents without environmental disadvantages, and performs overall process without the need of energy input. In method, ash content, preferably salt content of the resulting biomass is low (and meets current and future standards for solid fuels).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) solid biomass-derived fuel, obtained by the above-mentioned method; and    (2) biomass treated by the above-mentioned method.
NOVELTY - Continuous process for making fatty acids from a feedstock comprising phytoplankton in water, is claimed, where the weight content of the biomass in the slurry is less than 1 wt.% up to 35 wt.%.    USE - The process is useful for making fatty acids from a feedstock consisting of phytoplankton in water, where the fatty acid product is useful as a catalyst for enhancing the hydrolysis reaction, and the phytoplankton is useful as a food ingredient (all claimed) for human or animal consumption, and for making biofuels including biodiesel including methyl ester and ethyl ester, biolubricants including higher alkyl esters, green diesel, biojet fuels and fatty alcohols.    ADVANTAGE - The process provides fatty acids with improved physical and chemical properties in an economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a small amount of hydrogen (1.5 wt.% of the fatty acid content in the phytoplankton feed) that is injected along with the high pressure steam to support the hydrogenation reactions in the reactor; and    (2) high pressure steam that are injected into the hydrolysis reactor in the co-current flow mode with the preheated incoming slurry, recycled fatty acid product and hydrogen at three injection points to keep the reactor temperature at the required reaction conditions.
NOVELTY - Disinfecting sludge comprises adding burnt lime CaO to the sludge; agitating sludge mixture until the pH of the mixture is above 11; adding peroxide to the mixture to bind ammonia formed in the agitation step.    USE - Disinfecting method of sludge, preferably purification plant sludge from wastewater facilities or outlet sludge from biogas facilities (claimed).    ADVANTAGE - Pathogenic microbes, such as Escherichia coli and Salmonella, are disinfected out of the sludge in a way that the treated sludge measures up to official standards. Part of the ammonia released in the treatment is also bound into water soluble nitrogen compounds remaining in the treated sludge and thus improving the nutritional properties of the sludge. The method speeds up and enhances the treatment of sludge at the facilities, thus saving logistics costs because intermediate storing is not necessary. The sludge purified by the method does not contain harmful microbes and is of economic value as a soil amendment and a fertilizer due to the soluble nitrogen it contains. Equipment costs are low and the monitoring of the hygienization process is easy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for soil amendment and fertilizer produced by above method.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram illustrating the sludge disinfecting method.    Mixing tank (1)    Burnt lime dosage tank (2)    Peroxyacid dosage tank (3)    Outlet sludge conduit (4)    Silo (5)
NOVELTY - A cyclization of an uncyclized raw material compound (I) is carried out with condensing agent chosen from polyphosphoric acid, orthophosphoric acid, and concentrated sulfuric acid in the presence of one or more organic solvents chosen from 1,1,2-trichloroethene, methyl cyclohexane, cyclohexane, n-heptane, acetonitrile, 1,2-dimethoxyethane, 1,4-dioxane, tetrahydrofuran, N,N-dimethylformamide, ethyl acetate and methyl ethyl ketone, to obtain compound (II).    USE - Production of zaltoprofen or its derivative (claimed).    ADVANTAGE - The zaltoprofen or its derivative is economically produced with high yield without generating detectable amounts of dimer or other such impurities and polluting the environment, by simple method.    DETAILED DESCRIPTION - A cyclization of an uncyclized raw material compound of formula (I) is carried out with condensing agent chosen from polyphosphoric acid, orthophosphoric acid, and concentrated sulfuric acid in the presence of one or more organic solvents chosen from 1,1,2-trichloroethene, methyl cyclohexane, cyclohexane, n-heptane, acetonitrile, 1,2-dimethoxyethane, 1,4-dioxane, tetrahydrofuran, N,N-dimethylformamide, ethyl acetate and methyl ethyl ketone, to obtain compound of formula (II).    R1,R2=H or 1-8C hydrocarbyl.
NOVELTY - Extracting, distilling and separating butane and butylene by using ternary mixed solvent, is claimed. The ternary mixed solvent is N-methylpyrrolidone, methyl ethyl ketone and water.    USE - The method is useful for extracting, distilling and separating butane and butylene by using ternary mixed solvent (claimed).    ADVANTAGE - The method utilizes ternary mixed solvent which has high selectivity for butane and butylene, good solubility for 4C compounds, and low boiling point.
NOVELTY - Preparation of biomass coal char comprises drying biomass materials, crushing, pressing and forming, pyrolyzing and gasifying, and cooling to obtain biomass char; crushing, uniformly mixing biomass char, coal and binder at ratio of 20-40:50-70:10-20, and pressing.    USE - Method for preparing biomass coal char (claimed).    ADVANTAGE - The coal char is easy to burn and not easy to form slag after burning; has high mechanical strength and high calorific value, and does not produce black smoke during combustion process.
NOVELTY - A cooking gas produced from waste material of marshland.    USE - As a cooking gas (claimed).    ADVANTAGE - The cooking gas can be used as an alternative energy; saves environment from pollution; has low cost, thus some people get some benefit to earn money; is suitable to use for poor people because of this low cost; and can get market in our country and other country in the world because it is moving machine i.e. it can be move anywhere.
NOVELTY - Making a cherokee rose fruit saponin monomer, involves extracting crushed dried cherokee rose fruit peel by using organic solvent, decompressing and concentrating extracting solution, passing concentrated solution to high speed centrifugation or filtration under the low temperature, where the filtrate is macroporous absorption resin, collecting 30-60% aqueous ethanol solution, decompressing and recycling the solvent, drying the precipitate to obtain crude cherokee rose fruit saponin monomer, after 2-3 times recrystallization, refining to obtain pure cherokee rose fruit saponin monomer.    USE - For the preparation of a cherokee rose fruit saponin monomer (claimed).    ADVANTAGE - The method is simple; saves the dosage of the solvent; and is suitable for industrial mass production. The obtained cherokee rose fruit saponin monomer is safe to use.
NOVELTY - A biomass dry distillation kettle cover device, comprising a joint flange, a reinforcing rib, a centre ring and the cover main body. Cover main body is the utility model the one kind of biomass dry distillation kettle cover of the main body, the whole body is a disc-shaped structure, the upper part on the outer surface of the main body is uniformly provided with six reinforcing ribs of the cover main body in the middle position of the facing cutter is equipped with a central pull ring, the cover on the main body is provided with a joint flange and a temperature display device of the same. Here is provided with three the same in the form of a joint flange, increases the connection of a flexibility and also so as to increase the operation flexibility of the biomass destructive distillation kettle. This utility model is the one kind of biomass dry distillation kettle cover device, the whole structure is simple, convenient operation and use, good stability and high reliability. Using this utility model the one kind of the biomass dry distillation kettle cover device can ensure the heat conducting effect of the dry distillation kettle, the organic biomass thoroughly decomposing, and decomposing dry distillation kettle for specific operation.
NOVELTY - This utility model claims a measuring voltage of the electrolysis water electrolysis hydrogen plastic pole frame electrode plate, the electrode plate comprises a metal main electrode plate, an electrolytic voltage measuring column (for short measuring single column) electrode frame and the engineering plastic, engineering plastic electrode frame covered on the main board, so as to measuring column is embedded engineering plastic electrode frame, wherein measuring the first column of the main electrode plate, and measuring the other end passes through the column electrode engineering plastic frame is exposed. By pressing, injection molding, welding and injection moulding, and it can be prepared into measuring cell voltage of the plastic outer frame electrode plate. This utility model is novel compared a traditional metal electrode plate, it not only has a metal electrode plate through electrolysis voltage capable of measuring the characteristic of plastic product has excellent electric insulating performance. The adopted post test process is simple, and the main electrode plate is convenient to weld, it will not cause the main electrode plate is welded to deform and so on, can detect the electrolytic voltage of each electrolysis chamber, and is embedded in the plastic plate electrode frame can be accurately located according to the design, is a good sealing performance, no leakage.
NOVELTY - A bio-diesel preparing method involves reacting crude sulfate soap with 1-6C alkanol in presence of catalyst e.g. acid catalyst, and acetylchloride.    USE - Bio-diesel preparing method.    ADVANTAGE - The method enables preparing the bio-diesel by consuming less energy in a simple and inexpensive manner.
NOVELTY - This utility model claims a biomass fuel particle manufacturing equipment technology field, especially a kind of new biomass grain forming pressing material mechanism. It comprises transmission shaft driven by the motor, the upper part is provided with a plurality of outlet forming hole, pressing roller is provided with a plurality of outlet is frustum-shaped extruding head on the ring module on the transmission shaft and a pressing roller, a ring module is driven to rotate by the transmission shaft. This utility model uses the traditional pressing material pressing roller of ring mould forming machine of gear is changed into the frustum-shaped of a straight tooth or inclined tooth, so that pressure roller to rotate on the ring die, material extruding head can be well formed with the hole, the sliding force effect is obvious, the biomass of the volume is further reduced, the density is further improved, at the same time, provided with the auxiliary drive cover is covered on the upper part of the ring and the transmission shaft to rotate synchronously so that the pressure roller is further reduced when the resistance in the rotary pressing process, in addition, pressing roller is set, which is more helpful for pressing roller to keep balance in the rotating process, the structure is simple and the efficiency is high, it has strong practicability.
NOVELTY - This utility model claims a kind of inclined plate circulating fluid bed boiler burning biomass fluidized bed gasification device of biomass particle storage bin is connected with the spiral conveyer, a drying cyclone separator and the material, the lower the material cyclone separator connected with biomass storage bin, biomass storage bin and biomass fluidized bed inclined plate, inclined plate biomass fluidized bed on the upper part of the storage bin is connected with the lower part is connected with a bed material storage bin, the upper bed material storehouse is connected with bed material conveying pipe, heating the lower part of the conveying pipe is provided with a flue gas heating furnace, heating with a bed material storage bin, a bed material storage cabin part is provided with solid carbon powder and solid material cooling device, a material cyclone separator through pipeline is connected with a centrifugal fan and a cyclone separator. The device is mainly a set of device and gasification of biomass particle cooling and liquefying. The biomass is provided with a particle bed material in a uniform, heat transmission and mass transfer coefficient is high, the yield is high, it is easy to control, the reaction capacity and so on.
NOVELTY - The method comprises adding molecular oxygen to water to generate ozone by applying a voltage, and removing a portion of the ozone using a catalytic reduction unit. The method is performed by an electrolysis device such as a proton exchange membrane electrolyzer that is operated at a voltage of 2.3 V.    USE - The method is useful for electrolytic decomposition of water into hydrogen and oxygen (claimed).    ADVANTAGE - The method enables electrolytic decomposition of the water into hydrogen and oxygen with high yield in an effective and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolysis device.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an electrolysis device.    Electrolyzer (2)    First outlet (3)    Second outlet (5)    Unit for removal of ozone (6)    Oxygen outlet. (9)
NOVELTY - The method involves performing denitrifying process of the nitric acid containing wastewater biologically with an activated sludge. The oxidative decomposition treatment of the organic substance is performed. The iron content containing wastewater generated in iron mill is added in denitrifying treatment process and the organic substance decomposition process.    USE - Processing method of nitric acid containing waste water generated in iron mill.    ADVANTAGE - The solid-liquid separation property can be improved reliably. The rationalization of the wastewater treatment in the iron mill can be attained effectively. The settleability of sludge can be improved at low cost efficiently. The waste water treatment can be performed efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing apparatus of nitric acid containing wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the processing method of nitric acid containing wastewater.    Nitric acid containing wastewater treatment equipment (1)    Iron content containing wastewater supply apparatus (4)    Denitrifying tank (7)    Aerator (9)    Sedimentation tank (11)
NOVELTY - The equipment has reaction mixture supply devices (Zs1-Zs4) arranged adjacent to gas inlet and gas outlet of each gas treatment reactors (2-5). The reaction mixture outlet of gas treatment reactor (2) is connected with treatment unit (6) while reaction mixture outlets of other gas treatment of reactors (3-5) are connected with fertilizer treatment unit (7). A water electrolysis unit is directly connected with combined heat and power (CHP) station by oxygen line and with methane reactor (9) by hydrogen line, such that methane produced from methane reactor is supplied to CHP station.    USE - Equipment for chemical and energy recycling of flue gas emitted from power plant, incinerator, cogeneration plant, gas turbine, cement industry and other industries.    ADVANTAGE - The complexity in chemical and energy recycling of flue gas is reduced so that the chemical and energy recovery of flue gas is achieved.    DESCRIPTION OF DRAWING(S) - The drawings show a schematic view of the equipment for chemical and energy recycling of flue gas.    Heat exchanger (1)    Gas treatment reactors (2-5)    Treatment unit (6)    Fertilizer treatment unit (7)    Methane reactor (9)    Reaction mixture supply devices (Zs1-Zs4)
NOVELTY - Hydrogen generating apparatus (100) consists modifier (1) which produces hydrogen-containing gas by reforming reaction using raw material, hydrodesulfurization device (2) which removes sulfur compound present in the raw material supplied to the modifier, recycle flow path (6) which supplies a portion of hydrogen-containing gas discharged from the modifier to raw material before flowing into the hydrodesulfurization device, switching device (4) and controller (7).    USE - Hydrogen generating apparatus is used for fuel cell system (claimed).    ADVANTAGE - The hydrogen generating apparatus has excellent efficiency for generating power.    DETAILED DESCRIPTION - Hydrogen generating apparatus consists modifier which produces hydrogen-containing-gas by reforming reaction using raw material, hydrodesulfurization device which removes sulfur compound present in the raw material supplied to the modifier, recycle flow path which supplies a portion of hydrogen-containing gas discharged from the modifier to the raw material before flowing into the hydrodesulfurization device, switching device which switches whether hydrogen-containing gas supplied to the recycle flow path when the hydrogen concentration in a raw material exists in density (d1) and controller for controlling switching device such that the hydrogen-containing gas is not supplied to recycle flow path when hydrogen concentration in a raw material exists in density (d2) is more than hydrogen concentration in a raw material exists in density (d1). An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of hydrogen generating apparatus.    Modifier (1)    Hydrodesulfurization device (2)    Switching device (4)    Recycle flow path (6)    Controller (7)    Hydrogen generating apparatus (100)
NOVELTY - The fuel cell (1) has an electrode side electrical power collector (19c) that is positioned at other side of a sheet element (19a) and connected an electrode (15) with sheet element while a connector side electrical power collector (19b) is positioned at one side of sheet element and connected a connector (12) with sheet element. The main portion is arranged such that connector side electrical power collector and the electrode side electrical power collector are not overlapped, when collectors are seen along thickness direction of a cell main portion (3).    USE - Fuel cell for generating and supplying electric power.    ADVANTAGE - Since the main portion is arranged such that connector side electrical power collector and the electrode side electrical power collector are not overlapped, when collectors are seen along thickness direction of the cell main portion, the stress can be relieved when the current collection element transforms according to the displacement of the space of the cell main portion and the connector. Thus, the fuel cell which can maintain the favorable electrical connection property can be provided. The fuel cell can be used for long-time.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the fuel cell. (Drawing includes non-English language text)    Fuel cell (1)    Cell main portion (3)    Connector (12)    Electrode (15)    Sheet element (19a)    Connector side electrical power collector (19b)    Electrode side electrical power collector (19c)
NOVELTY - Method for producing compost, involves mixing some organic waste derived from animals and plants to produce compost raw material, stirring the compost raw material with part of compost raw materials fermented previously, carrying out stationary storage of the compost raw material for every production stage, and reversing the compost raw material based on temperature change of the compost raw material, repeating the storage process and inversion process for multiple times, and fermenting the compost raw material while supplying part of compost raw materials.    USE - The method is useful for producing compost (claimed), used for greenhouse cultivation.    ADVANTAGE - The method utilizes various organic wastes and less time and is cost-effective.    DETAILED DESCRIPTION - Method for producing compost, involves mixing some organic waste derived from animals and plants to produce compost raw material having moisture content of 55-80 wt.%, stirring the compost raw material with part of compost raw materials fermented previously, carrying out stationary storage of the compost raw material for every production stage, and reversing the compost raw material based on temperature change of the compost raw material, repeating the storage process and inversion process for multiple times, and fermenting the compost raw material while supplying part of compost raw materials. An INDEPENDENT CLAIM is included for compost manufacturing plant.
NOVELTY - Processing organic substrates into fertilizers, comprises subjecting the substrate to aerobic process in the presence of effluent, biogas and moist oxygen-containing gas, heating and hydrolyzing the substrate, separating the substrate into fractions, and liquid fractioning the substrate, where the effluent is used as heat transfer agent for adjusting a thermal mode in aerobic process, and as ammonium nitrogen source for concentration of solid fraction, and the moist oxygen-containing gases are used for preheating and aerating the initial substrate.    USE - The method is useful for processing organic substrates into fertilizers and gaseous energy carrier (claimed). No biological data given.
NOVELTY - An ionic fuel generating system for producing hydrogen and oxygen comprising an electrolyzer chamber for containing water mist, electrodes fitted in the chamber and a dc power source connected to the electrodes to effect the electrolytic process of the contained water mist thereby slitting the hydrogen and oxygen components thereof.    USE - For producing hydrogen and oxygen.
NOVELTY - Enzyme saccharification of cellulose biomass feedstock is performed by preparing slurry containing cellulose biomass feedstock, calcium hydroxide, and water which are cut out, pulverized, ground, or mashed, performing alkali treatment with respect to raw material, separating into solid and liquid, adjusting pH to 5-8 by neutralizing using carbon dioxide with respect to solid substance obtained by solid-liquid separation or mixture of solid substance and water, and carrying out enzyme saccharification reaction.    USE - Enzyme saccharification of cellulose biomass feedstock for collection of useful compounds (claimed).    ADVANTAGE - Efficiency of enzyme saccharification is improved, generation of salt with difficult waste processing does not occur, and process cost reduction is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for collection of compound from cellulose biomass feedstock which involves performing extraction and/or purification process with respect to solid substance and separating liquid by solid-liquid separation.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the result of measuring the amount of ferulic acid extracted from alkali-treated material of cellulose biomass feedstock. (Drawing includes non-English language text).
NOVELTY - The system has an anaerobic digester tank (18) that disassembles the solid material that is applied from a centrifugal concentrator (14). A solubilization unit (16) performs solubilization of portion of thickened sludge that is generated in the centrifugal concentrator on which the residual sludge that is ejected from a bio-reaction turning point of separating membrane is concentrated. A membrane bioreactor (12) has a separation film that separates the solid from liquid, disassembles the organic compounds, and generates the methane gas.    USE - System for generating biogas from sludge in sewage treatment plant.    ADVANTAGE - The cost is reduced and the efficiency is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biogas generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas generation system. (Drawing includes non-English language text)    Membrane bioreactor (12)    Centrifugal concentrator (14)    Solubilization unit (16)    Anaerobic digester tank (18)    Dehydrator (20)
NOVELTY - The reactor device comprises multi-configurable two electrodes (100) and a dividing element (120), where the dividing elements form a chamber (136) for accommodating fluid to be separated when each mounted between multi-configurable two electrodes. The multi-configurable electrode is made from a conductive material which cutting direction provides making sense of their crystalline formation. The conductive material is non-ferrous or semi-conductive. The multi-configurable electrode has electric-electronic connection terminal (106,110), and one or multiple feed holes (112) and outlet holes.    USE - Reactor device for molecular dissociation of fluids.    ADVANTAGE - The reactor device comprises multi-configurable two electrodes and a dividing element, where the dividing elements form a chamber for accommodating fluid, and thus simply separates a fluid used as a source into various component elements.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic exploded perspective view of elements of the reactor device.    Electrodes (100)    Connection terminal (106,110)    Feed holes (112)    Dividing element (120)    Chamber (136)
NOVELTY - The circulating fluidized bed biomass gasifier comprises a long straight type fluidized-bed gasification unit arranged in a lower surface of an air inlet door, a raw material storage unit arranged on one side of the fluidized bed gasification unit, an air distribution plate that is placed on an upper part of an air inlet unit and includes a residue outlet and an inverted cone-shaped air entry chamber, a straight raw material supply pipe, a circulating pipe and a backflow L valve, and a screw material feeder.    USE - The circulation fluid bed biomass gasifier such as a pyrolysis gasifier is useful in industrial boilers for oil and gas combustion.    ADVANTAGE - The fluid bed biomass gasifier exhibits stable and high gasification efficiency.
NOVELTY - The apparatus comprises a sample ejector for ejecting a sample with less water content, a first and a second magnetron for microwave irradiation of the sample, first and second heating units for hearing the sample, a dryer, a first outlet pipe, and a second discharge pipe for discharging semi-carbonized sample. The second heating unit comprises semi-carbonizing unit. The first outlet pipe includes an outlet connected to the drier. The first and second heating units are connected to each other. A cylindrical opening is positioned on a side of the dryer for inflow of outside air.    USE - The apparatus is useful semi-carbonizing a sample using microwave energy (claimed).    ADVANTAGE - The apparatus allows semi-carbonization of the sample with less energy consumption in a rapid and economical manner.    DETAILED DESCRIPTION - The apparatus comprises a sample ejector for ejecting a sample with less water content, a first and a second magnetron for microwave irradiation of the sample, first and second heating units for hearing the sample, a dryer, a first outlet pipe, and second discharge pipe for discharging semi-carbonized sample. The second heating unit comprises semi-carbonizing unit. The first outlet pipe includes an outlet connected to the drier. The first and second heating units are connected to each other. A cylindrical opening is positioned on a side of the dryer for inflow of outside air. The first and second discharge pipes comprise an impeller. The impeller prevents flow of the air to the dryer, and the semi-carbonizing unit performs carbonization of the sample. The sample is put into the drier. The sample is semi-carbonized using microwave as an energy source. The apparatus further comprises a boiler. The heating units include heating oil used as a heating medium. The boiler is heated by the heating unit.
NOVELTY - The device has a material input device (20), and a continuous input unit that receives charcoal that falls down from a grating. A fire extinguisher system (40) has a tank (41), and a vent is provided in the lower side of the tank. An exhaust apparatus has a rotary plate that ejects the charcoal through the vents. The center portion of grating is vacant, and a water cooling jacket (17) is formed on the lower side of a furnace (10). A rotator is formed in the upper end of a rotary shaft. A hot air chamber (50) and a ventilation hole (52) are formed in the furnace.    USE - Device for manufacturing charcoal for fuel, for deodorant, and for as soil conditioner in agriculture.    ADVANTAGE - The loss of energy is reduced. The work hours are reduced and productivity is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the device for manufacturing charcoal.    Furnace (10)    Water cooling jacket (17)    Material input device (20)    Fire extinguisher system (40)    Tank (41)    Hot air chamber (50)    Ventilation hole (52)
NOVELTY - An acidogenic reactor system has an inhibitor chosen from volatile fatty acid and hydrogen which regulates microbial population.    USE - Acidogenic reactor system is used for generating biogas (claimed).    ADVANTAGE - The acidogenic reactor system efficiently improves capture of carbon dioxide and energy recovery from anaerobic digestion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of generating biogas using acidogenic reactor system, which involves seeding acidogenic reactor with anaerobic sludge as seed from existing anaerobic system, adding anaerobic sludge to acidogenic reactor in sequential batchwise or continuous process, maintaining pH within acidogenic reactor to 5-5.5 and at 30-50 degrees C, manipulating concentration of inhibitor chosen from volatile fatty acid and hydrogen in acidogenic reactor to regulate microbial population, optionally recycling produced biogas within acidogenic reactor to acidogenic reactor for further reaction and transferring treated anaerobic sludge to downstream reactor; and    (2) usage of volatile fatty acid and/or hydrogen to regulate microbial population of acidogenic reaction.
NOVELTY - Low cost pre treatment process for press mud which ensures round the year availability of press mud to recover its optimum energy potential and increases the shelf life by preventing it from microbial and/or fungal attack.    USE - The low cost pre treatment process is useful for press mud (claimed). Preferably, it can be used as anaerobic process for producing organic manure and/or biogas from substances such as press mud from sugar mills, agricultural and/or industrial wastes.    ADVANTAGE - Low cost pre treatment process for press mud which ensures round the year availability of press mud to recover its optimum energy potential and increases the shelf life by preventing it from microbial and/or fungal attack, is provided (claimed). The effective heat treatment makes it possible to recover energy potential of press mud. Extended shelf life of this waste allows downsizing the bio-methanation plant and ensuring its round the year operation without efficiency loss. Reduction of bio-methanation plant size reduces the capital cost of the plant and hence makes the process more economic. Heat drying of the waste before storage makes it more eco-friendly. Pretreatment results in reduced cost of storage and transportation of the waste. The treatment costs are considerably less compared to the extended gas generation potential of the feed.
NOVELTY - An isolated Tetraselmis suecica (BEA D0111) is new.    USE - The T. suecica (BEA D0111) or microalgae population is useful for producing biofuel selected from biodiesel and hidrobiodiesel (all claimed).    ADVANTAGE - The T. suecica (BEA D0111) has higher lipid content, increased cell size and higher growth rate than other strains. The strain is used for low cost and high yield biodiesel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a microalgae population comprising the T. suecica (BEA D0111) above; and (2) a process for producing biofuel by (a) culturing the T. suecica (BEA D0111) or microalgae population, (b) removing the fatty acids produced in step (a), and (c) conducting a transesterification process or the hydrogenation of fatty acids extracted in step (b).
NOVELTY - Producing sugar and/or bioethanol from biomass comprises (a) a main method for producing bioethanol and/or sugar; (b) a secondary method for producing biofuels and/or chemical products from bioethanol and/or the by-products of the production of bioethanol; where the main method for producing bioethanol includes: (c) obtaining a diffusion juice from the biomass used as a raw material, the diffusion juice being separated from a residue or pulps; and (d) subjecting the diffusion juice obtained in the preceding step to fermentation process followed by distillation and dehydration.    USE - The method is used for producing sugar and/or bioethanol from biomass (claimed).
NOVELTY - This utility model claims a kind of high strength adhesive of glass fibre reinforced methane tank, comprising a tank cover and a lower semi-ellipsoidal, the upper cover and the lower pool are provided with a flange, the flange is provided with a ring of high strength fibre with the upper cover by a flange of the lower pool. A current glass steel marsh gas tank, the utility model using the high strength fibre belt on the flange edge, and is connected with the upper cover, the lower pool body SMC sheet integral moulding is that the glass steel marsh gas tank upper cover, under the pressing and greatly improve the marsh gas pool of the pool cover and the lower flange of the integral intensity, avoid the truck loading and unloading, transporting and mounting process flange by collision and so on generate micro-crack. High-strength Fibre belt overcomes the extending and expanding the crack, wherein the high strength fibre belt, further can according to need, adding the glass fibre reinforced plastic biomass pool and the upper cover, the other part of the lower pool, so as to meet the strength requirement, provide a solid foundation is glass fibre reinforced plastic marsh gas tank and the upper cover, extended use of the lower pool.
NOVELTY - The method involves condensing tail gas and liquid acetic acid so as to perform gas condensation, where the condensation of the gas is arranged in contact with liquid. The tail gas is placed in a gas acetic acid raw material tank, where the tail gas is formed of sec-butyl acetate and C4 hydrocarbon, which comprises n-butane and isobutene, and mass ratio of the acetic acid and non-condensed gas is greater than 1.    USE - Method for processing tail gas.    ADVANTAGE - The method enables a user to process the tail gas in an inexpensive manner.
NOVELTY - A catalyst is scandium-enhanced coprecipitation type nickel-cobalt-based catalyst (I). The catalyst comprises 48-62 wt.% nickel, 3-25 wt.% scandium and remainder of zirconium.    USE - Catalyst is used for preparing synthetic natural gas.    ADVANTAGE - The catalyst has high stability, and excellent heat resistance. The conversion rate of hydrogenated methanation of carbon monoxide and carbon dioxide and yield of product (methane) are effectively improved.    DETAILED DESCRIPTION - A catalyst is scandium-enhanced coprecipitation type nickel-cobalt-based catalyst of formula: NiiZrjSck (I), where i, j and k are molar ratio coefficient of nickel, zirconium and scandium in the catalyst. The catalyst comprises 48-62 wt.% nickel, 3-25 wt.% scandium and remainder of zirconium. An INDEPENDENT CLAIM is included for preparation of catalyst, which involves mixing hexahydrated nickel nitrate, trihydrated zirconium nitrate, and scandium nitrate into aqueous solution, carrying out coprecipitation reaction with potassium aqueous solution, filtering feed liquid after reaction, cleaning, drying, and baking filtered cake.
NOVELTY - A wheat straw pulp refining method involves softening wheat straw, and extruding straw soaking solution. The wheat straw is dehydrated, washed and reacted with disodium edetate, sodium borohydride and hydrogen peroxidase in a thread rolling machine. Wheat straw pulp is prepared through a medium-concentration grinding machine and a high-concentration grinding machine. The wheat straw pulp is stirred and diluted, and a broom thread separation is performed. A final product is prepared through the medium-concentration grinding machine and the high-concentration grinding machine.    USE - Method for refining wheat straw pulp.    ADVANTAGE - The method enables reusing pulping water and biological dissolution solution for soaking the wheat straw and avoiding production and emission of black liquor.    DETAILED DESCRIPTION - A wheat straw pulp refining method involves softening wheat straw by adopting 16-20 wt.% sodium hydroxide and 0.6-0.9 wt.% sodium sulfite for cold soaking, and extruding a straw soaking solution through a screw extruder. The wheat straw is dehydrated, washed and reacted with 0.5-2 wt.% disodium edetate, 0.1-0.3 wt.% sodium borohydride and 0.5-1.39 wt.% hydrogen peroxidase in a thread rolling machine for fibrillation. Wheat straw pulp is prepared through a medium-concentration grinding machine and a high-concentration grinding machine. The wheat straw pulp is stirred to dissolve and diluted to 1x 10-4 g/l, and a broom thread separation is performed at 75-120 degrees C for 15-25 min. A final product is prepared through the medium-concentration grinding machine at 65 plus minus 5 degrees C for 5-12 min and the high-concentration grinding machine at 55 plus minus 5 degrees C for 5-12 min.
NOVELTY - Method for removing heavy metal involves adsorbing metal adsorbent and biogas into a pond, stirring, then allowing to stand, providing supernatant into buffer upgrade biogas tanks, adding secondary batch to be purified biogas slurry, stirring, roasting heavy metal adsorbent-modified diatomaceous earth, providing commercially adsorbent clay-based ceramic, removing heavy metal, adsorption filtering, purifying water, discharging biogas safety irrigation, and recycling and absorbing agent zeolite acid modified.    USE - Method for removing heavy metal in biogas slurry (claimed).    ADVANTAGE - The method efficiently removes heavy metal in biogas slurry with reduced energy consumption without polluting the environment, by simple method.    DETAILED DESCRIPTION - Method for removing heavy metal involves adsorbing metal adsorbent and biogas into a pond in the ratio of 1:100, stirring for 0.5-1 hour, then allowing to stand for 0.5-1 hour, then providing supernatant into a buffer upgrade biogas tanks, lifting precipitation in the bottom of pool to be ranked adsorption, adding secondary batch to be purified biogas slurry, stirring, roasting heavy metal adsorbent-modified diatomaceous earth, absorbing buffer lifting upper clear liquid to the secondary absorbing tank, providing main tank with a clay ceramsite of adsorption filtration layer, flowing slurry into three adsorption adsorption filtration pond, providing commercially adsorbent clay-based ceramic, filling adsorption tanks with a modified zeolite fillers, removing heavy metal, adsorption filtering, purifying water, discharging biogas safety irrigation, and recycling and absorbing agent zeolite acid modified. An INDEPENDENT CLAIM is included for device.
NOVELTY - Preparation of arginine-ibuprofen crystal involves reacting ibuprofen and arginine at 10-40 degrees C in aqueous solution of solvent acetone to form salt, adding acetone into obtained supersaturated solution to separate out arginine-ibuprofen crystal from supersaturated solution, stirring, removing water at 10-40 degrees C to form uniform suspended material to obtain nearly-anhydrous crystal, washing crystal using acetone, and drying. The molar ratio of ibuprofen and arginine is 0.95-1.2:1. The acetone is dripped into the supersaturated solution at dripping speed of 20-500 ml/minute in 1000 ml.    USE - Preparation of arginine-ibuprofen crystal used for pharmaceuticals.    ADVANTAGE - The arginine-ibuprofen crystal is manufactured efficiently and economically with reduced energy consumption.
NOVELTY - A carbon dioxide natural gas replacement emulsion utilization method reducing pressure of natural gas hydrate. Carbon dioxide is added into the natural gas hydrate. Carbon dioxide natural gas replacement emulsion is injected to perform a replacement reaction. Methane is recovered from a gas well when gas content of each component in the natural gas hydrate storage layer is stable. The carbon dioxide natural gas replacement emulsion is composed of carbon dioxide, two types of surface active agent, hydrate growth inhibitor and water.    USE - Method for utilizing carbon dioxide natural gas replacement emulsion to replace methane in natural gas hydrate formation.    ADVANTAGE - The method enables utilizing carbon dioxide natural gas replacement emulsion in a simple and efficient manner.    DETAILED DESCRIPTION - A carbon dioxide natural gas replacement emulsion utilization method reducing pressure of natural gas hydrate. Carbon dioxide is added into the natural gas hydrate. Carbon dioxide natural gas replacement emulsion is injected to perform a replacement reaction. Methane is recovered from a gas well when gas content of each component in the natural gas hydrate storage layer is stable. The carbon dioxide natural gas replacement emulsion is composed of carbon dioxide, two types of surface active agent, hydrate growth inhibitor and water, where the surface active agent comprise sodium sulfate whose mass percentage concentration is 0.0001-1%, mass percentage concentration of other surface active agent is 0.10-10.0%, mass concentration of hydrate growth inhibitor is 50.0%, volume percentage of water is 10-90% and the volume percentage of carbon dioxide is 10-90%.
NOVELTY - The shipment building comprises a liquefied fertilizer reservoir, a liquefied fertilizer fermenter, a layer for removing an odor, a chamber for reducing odor, an odor flow passage, a nozzle pipe and a filter. The liquefied fertilizer is supplied to the chamber for reducing the odor in the fertilizer using the odor flow passage. The chamber includes first and second barriers and inlet and outlet ports. The liquefied fertilizer is further supplied to the fermenter using the nozzle pipe.    USE - Used as a shipment building having an odor removing function.    ADVANTAGE - The shipment building removes the odor in an economical and efficient manner.    DETAILED DESCRIPTION - The shipment building comprises a liquefied fertilizer reservoir, a liquefied fertilizer fermenter, a layer for removing an odor, a chamber for reducing the odor, an odor flow passage, a nozzle pipe and a filter. The liquefied fertilizer is supplied to the chamber for reducing the odor in the fertilizer using the odor flow passage. The chamber includes first and second barriers and inlet and outlet ports. The liquefied fertilizer is further supplied to the fermenter using the nozzle pipe. A bottom opening part is located in the first barrier. The odor flow passage is formed in a lower part. The reservoir includes a shipment layer, an odor removing mechanism, and a liquefied fertilizer shipment tub. The filter includes a moisture interception filter, which ejects air to the outside.
NOVELTY - A silicon dioxide film comprises two structural layers having an alpha-aluminum oxide porous ceramic supporting body and a silicon dioxide top layer separation film material, where the diameter of the film aperture is 18-30 nm and average pore size is 21 nm.    USE - Silicon dioxide film for separating methane and carbondioxide gas.    ADVANTAGE - The silicon dioxide film has higher selectivity and high gas separation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a silicon dioxide film, which involves pretreating supporter aluminum oxide de-ionized water and carrying out ultrasonic cleaning for 30 minutes, Preparing silica sol by adding ethyl orthosilicate and de-ionized water, dropping in catalyst at 70 degrees C, stirring under magnetic force for 3 hours to obtain the sol grain of silicon dioxide sol-gel, preparing mesoporous silicon dioxide film by multiple separate coating processes, preparing silicon dioxide sol by Dip-coating process, coating silicon dioxide sol on the pre-processed aluminum oxide supporting film-forming, carrying out calcining, coating film, and drying, where the calcining process is repeated for 4-5 times to obtain the non-defective mesoporous silicon dioxide film.
NOVELTY - A catering industry waste oil-based biological alcohol oil comprises 35-55 wt.% methanol, 30-50 wt.% pretreated catering industry waste oil, 1-3 wt.% alkali, 2-5 wt.% combustion promoter, 1-5 wt.% emulsifier, 0.5-1.5 wt.% catalyst, 2-5 wt.% cosolvent and 0.5-1.5 wt.% smell removal agent.    USE - Catering industry waste oil-based biological alcohol oil is used as liquid fuel in industrial and civil field.    ADVANTAGE - The catering industry waste oil-based biological alcohol oil does not self-ignite and volatilize easily, and is economical and environmentally-friendly. The catering industry waste oil-based biological alcohol has reduced petrifaction and mineral fuel consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catering industry waste oil-based biological alcohol oil. Catering waste oil is added into high speed centrifuge, centrifuged at the rotating speed of 500-700 rpm, and filtered to remove waste oil in the residual solid impurity. According to cohesion theory, the colloid removing catering waste oil is processed and dried to obtain pretreated waste oil. Catalytic agent and specified amount of oil/alcohol is added, and ester exchange reaction is performed. After adding alkali into the reaction mixture, the mixture is continuously stirred to carry out saponification reaction. Sodium hydroxide, potassium hydroxide and water are added to resultant mixture, stirred to dissolve completely in the container, and ethyl acetate is added. Remainder of methanol and combustion accelerator, emulsifier, latent solvent and smell-eliminating agent are added to the obtained reaction mixture, and stirred uniformly to obtain catering industry waste oil-based biological alcohol oil.
NOVELTY - Enriching anaerobic ammonium oxidizing bacteria from normal active sludge comprises performing nitration treatment on the common activated sludge under an oxygen-free condition to increase quantity of aerobiotic ammonium oxidation bacteria (AOB) in the sludge, further increasing the quantity of the AOB using hydroxylamine oxidoreductase, pouring activated carbon in an activity enhancement phase to improve attachment environment for AOB, and reducing the activated carbon using bacteria.    USE - The method is useful for enriching anaerobic ammonium oxidizing bacteria from normal active sludge (claimed).    ADVANTAGE - The method is capable of enriching anaerobic ammonium oxidizing bacteria from normal active sludge in a rapid and efficient manner.
NOVELTY - The device has conductive filler (7) which is connected with cathode chamber and anode chamber by a circuit, for illuminating the UV light. The current from the cathode chamber flows to anode chamber. The cathode waste water inlet (1) is provided at the bottom of the cathode chamber, and the top of cathode chamber is provided with a cathode water outlet (2). The anode chamber water inlet (3) is provided at the bottom of anode chamber, and the cathode chamber outlet is directly provided into anode chamber. The top of anode chamber is provided with an anode water outlet (4).    USE - Device for simultaneously performing wastewater treatment and power generation using photo-catalytic associated microbial fuel cell technology.    ADVANTAGE - The effect for removing the organic matter is increased under the dual effect of anode chamber and cathode chamber, so that nitrifying and denitrifying effect can be finished effectively. The device with simple structure can perform the sewage treatment with low cost and with low power.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for simultaneously performing sewage treatment and power generation using photo-catalytic associated microbial fuel cell technology.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for simultaneously performing wastewater treatment and power generation.    Cathode waste water inlet (1)    Cathode water outlet (2)    Anode chamber water inlet (3)    Anode water outlet (4)    Conductive filler (7)
NOVELTY - Recycling surplus sludge in a municipal sewage plant comprises concentrating the surplus sludge in a sewage treatment plant sedimentation and then reacting, crushing the residual sludge, processing the residual sludge into a microwave reactor, carrying out microwave radiation of the processed mixture to prepare a mixed solution, adding the obtained mixed solution and then centrifuging and separating, hydrolyzing the sludge by adding glucose and then stirring, inoculating the sludge hydrolysis solution culture medium by a hydrogen-producing microorganism to culture.    USE - The method is useful for recycling surplus sludge in a municipal sewage plant (claimed).    ADVANTAGE - The method economically recycles the surplus sludge with good hydrogen-producing effect.    DETAILED DESCRIPTION - Recycling surplus sludge in a municipal sewage plant comprises (1) concentrating the surplus sludge in a sewage treatment plant sedimentation to adjust a pH value of the concentrated sodium hydroxide solution to 12 and then reacting for 30-90 minutes, (2) crushing the residual sludge for 25 minutes under an ultrasonic condition, where the sludge has: a ultrasonic frequency of 20-44 KHz; ultrasonic intensity of 0.5-4 W/ml, (3) processing the residual sludge into a microwave reactor, carrying out microwave radiation of the processed mixture having a microwave power of 200-700 W for 1-10 minutes to prepare mixed solution, (4) adding the obtained mixed solution and then centrifuging, and separating the supernatant, (5) hydrolyzing the sludge by adding 1-20 g/l of glucose (10%) to adjust a pH value to 6.8-7 and then stirring under the protection of nitrogen atmosphere to obtain sludge hydrolysis solution culture medium, and (6) inoculating the sludge hydrolysis solution culture medium by hydrogen-producing microorganism at a temperature of 37 degrees C to culture for 36-48 hours.
NOVELTY - Waste methanol generated by biodiesel production is stored in storage tank in liquid phase. The stored product is pumped to negative-pressure flash tank. The methanol is concentrated to obtain crude methyl alcohol having concentration of more than 65%. The obtained product is pumped to rectifying tower, refined, refined product is recycled to biodiesel production process and bottom product of rectifying tower containing water-containing methanol is recycled to flash tank. Thus, recycling of waste methanol is carried out.    USE - Recycling of waste methanol (claimed).    ADVANTAGE - The method efficiently recycles waste methanol by simple and environmentally-friendly process with less consumption of energy.
NOVELTY - Preparation of N-alkyl aminophenol involves reacting 3-aminophenol and trialkyl orthoformate as raw materials and NAFION-H (RTM: resin) as catalyst under solvent at preset temperature and obtaining 3-ethylaminophenol, filtering 3-ethylaminophenol to remove the catalyst, condensing solvents, and carrying out reduced pressure distillation.    USE - Preparation of N-alkyl aminophenol (claimed).    ADVANTAGE - The method efficiently and economically provides N-alkyl aminophenol having conversion rate, selectivity, yield coefficient and purity under mild reaction temperature, without generating wastewater and waste gas.
NOVELTY - An automotive plateau-type modified fuel methanol contains 3-10 pts. wt. methanol-based clean fuel blending additives and 90-97 pts. wt. automotive fuel methanol.    USE - Automotive plateau-type modified fuel methanol is used for producing gasoline (claimed).    ADVANTAGE - When methanol gasoline blended with plateau-type modified fuel methanol is used, the increase of octane value is stable, a direct ratio relationship exists between additive amount and octane value, and combustion stability and storage stability of the fuel are improved. Methanol gasoline is not oxidized and deteriorates after long-time storage. The methanol gasoline blended with plateau-type modified fuel methanol has low emission, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of automotive plateau-type modified fuel methanol, which involves mixing methanol-based clean fuel blending additives and automotive fuel methanol in a static mixer.
NOVELTY - A methanol gasoline catalyst contains 20-40 volume% mutual solvent, 10-20 volume% combustion catalyst, 10-20 volume% thermal value enhancing agent, 25-30 volume% core mixtures, 1-5 volume% antioxidant anti-glue, 1-5 volume% metal deactivator, 1-5 volume% vapor pressure adjusting agent and 0.1-2 volume% rubber swelling inhibitor.    USE - Catalyst is used for producing methanol gasoline.    ADVANTAGE - The catalyst efficiently and economically forms methanol gasoline with high productivity, without changing engine structure. The methanol gasoline is powerful, and can be easily started at low temperature. Methanol gasoline has no gas block at high temperature, and can resist rubber swelling.
NOVELTY - Vegetable oil and low alcohol are added to 1,2,3-triazole carbene carbon dioxide adduct as catalyst, mixing, stirred uniformly and transesterification reaction is carried out to obtain biodiesel.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method efficiently and safely provides biodiesel having excellent catalyst stability and high reaction activity, under mild reaction conditions by simple method without affecting the environment.
NOVELTY - Desmodesmus sp. (ENN2203A), comprising a preservation number CGMCC No. 4323, is new.    USE - The Desmodesmus sp. is useful: in treating nitrogen and phosphorus containing sewage, reducing carbon dioxide emissions, and aquatic bait or animal feed; and for producing biodiesel (claimed).    ADVANTAGE - The Desmodesmus sp. has high temperature resistance; is easy to collect; has strong environmental adaptability; and is suitable for high density cultivation and industrial application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for culturing Desmodesmus sp., comprising culturing at 15-40 degrees C.
NOVELTY - Heat treatment combined preprocessing of surplus sludge containing short chain fatty acids comprises carrying out heat treatment to taking residual sludge of a sewage treatment plant, controlling the initial pH in order to control microbial activity to promote the dissolution of organic substances, allowing the hot pre-treated residual sludge to reside in the reactor, converting the insoluble organic substances into soluble organic substances by hydrolytic conversion, where the insoluble organic substance is short-chain fatty acid and soluble organic substance is protein or polysaccharide.    USE - The method is useful for heat treatment combined preprocessing of surplus sludge containing short chain fatty acids (claimed).    ADVANTAGE - The method reduces environmental pollution.    DETAILED DESCRIPTION - Heat treatment combined preprocessing of surplus sludge containing short chain fatty acids comprises taking residual sludge of a sewage treatment plant as a raw material, carrying out heat treatment at 60-120 degrees C for 15-60 minutes, controlling the initial pH to 8-12 in order to control microbial activity to promote the dissolution of organic substances in the residual sludge, allowing the hot pre-treated residual sludge to reside in the reactor for 1-12 days at 30-40 degrees C, converting the insoluble organic substances into soluble organic substances by hydrolytic conversion, where the insoluble organic substance is short-chain fatty acid, and the soluble organic substance is protein or polysaccharide.
NOVELTY - This utility model claims a movable biogas pool material liquid stirrer, wherein it comprises an air compressor, a gas-guide tube with the marsh gas pool gas outlet is connected with the air outlet of the air compressor, the air inlet pipe is set one another end of the vent pipe, the vent pipe is the air outlet of the air compressor, in the feeding port into marsh gas tank. This utility model using marsh gas circulating reflux cracking, immediately after the methane tank material liquid cracking, fast gas production, which avoids the air enter into marsh gas tank, at the same time the methane tank material liquid fermented active bacteria microorganism protected.
NOVELTY - This utility model claims a marsh gas generator, comprising a feeding chamber, a fermentation chamber, a discharging and collecting pipe, the feeding chamber, the fermentation chamber and a discharging chamber connected in turn, collecting pipe is connected with the fermentation chamber, a feeding chamber, a fermentation chamber, a discharging chamber is a cavity of the pipe-shaped structure is parallel paved on the ground. This utility model claims a marsh gas generator, a feeding chamber, a fermentation chamber, a discharging and collecting pipe is paved on the ground parallel to the pipe-shaped structure is connected to the marsh gas generator solves the problem that the occupied space is large;
NOVELTY - Sand and suspended materials are filtered from pig manure and wastewater, and treated material is hydrolyzed for removing chemical oxygen demand in wastewater. The treated materials are supplied to a fermenting chamber through a feeding pump to seal-ferment and obtain product biogas. Biogas is then treated in a gas-water separator and a desulfurizing tower device. Treated biogas is collected and sent to a gas storage cabinet, metered through a biogas flow meter, pressurized by a frequency conversion pressurizing device, and conveyed to a generator room.    USE - Production of biogas in large biogas project (claimed).    ADVANTAGE - The method effectively meets electricity requirements for production and living in farms, saves energy resource, improves environment and soil, enhances fertilizer effect, accelerates development of breeding industry, reduces labor intensity, and is environmentally-friendly.    DETAILED DESCRIPTION - Pig manure and wastewater are conveyed to a wastewater treatment station through pipe or transportation, and sand and suspended materials are filtered through a grid tank. Treated pig manure and wastewater are hydrolyzed in a hydrolysis acidification pool to dilute and stir for improving the biodegradability of wastewater and removing chemical oxygen demand (COD) in wastewater. The treated materials are supplied to a fermenting chamber through a feeding pump to seal-ferment and obtain product biogas. Biogas is then treated in a gas-water separator and a desulfurizing tower device. Treated biogas is collected and sent to a gas storage cabinet, metered through a biogas flow meter, pressurized by a frequency conversion pressurizing device, and conveyed to a generator room.
NOVELTY - A thick filter is pre-processed for catering oil or hogwash oil, and esterification is performed as catalyst for fatty acid side group metal organic compound, to obtain fatty acid polyol ester. The transesterification is performed, esterification of waste oil in the group IA or IIIA metal alcoholates as catalysts is catalyzed with methanol, fatty acid methyl esters and glycerol for 0.5-3 hours, standard and then washed by water, glycerine layer is separated, dealcoholization is performed, and distilled. The amount of group IA or IIIA metal catalyst is 0.2-0.6 wt.%.    USE - Production of biodiesel (claimed).    ADVANTAGE - The biodiesel is efficiently produced with high catalytic activity and yield, and reduced methanol consumption, and excellent quality.
NOVELTY - An efficient, improved and environmentally friendly process for the synthesis of dibenzo(1,4)thiazepine-11-(10H)-one by limiting the use of various solvents and hazardous Hydrochloric acid, to provide an easy to implement, cost effective and in good yield and purity using iron powder and ammonium chloride and ferric chloride.
NOVELTY - The present invention discloses a novel process for the preparation of the amorphous form of S-omeprazole magnesium trihydrate. The present invention also provides a new crystalline polymorph III of Magnesium salt of S-Omeprazole trihydrate and to the process for the preparation thereof. The novel process for the preparation of the amorphous as well as the crystalline form involves the use of a chelating agent having alkaline pH to chelate out the excess and magnesium ions from the reaction mixture to enable the direct precipitation of trihydrate of magnesium salt of S-omeprazole in good yield and purity.
NOVELTY - L-arginine fermentation liquid is filtered by membrane filtration. The obtained filtrate is supplied to ultra-filtration membrane, and purified liquid and concentrate are collected. The retentate and concentrated liquid are combined and dried, to obtain animal nutrition feed. The purified liquid is concentrated and ammonia is slowly added. The solution is isoelectric-deposited, centrifuged, precipitated, and precipitate, supernatant and mother liquor are collected. The precipitate is stirred in alcohol, washed, centrifuged, precipitated and dried, to obtain L-arginine.    USE - Production of L-arginine (claimed).    ADVANTAGE - The L-arginine having high purity is produced with high yield by simple method, without environmental pollution.    DETAILED DESCRIPTION - L-arginine fermentation liquid is filtered by membrane filtration to remove bacteria, and retentate and filtrate are collected. The filtrate is supplied to ultra-filtration membrane, and purified liquid and concentrate are collected. The retentate and concentrated liquid are combined and dried, to obtain animal nutrition feed. The purified liquid is concentrated for 5-10 times, slow cooled to 20 degrees C and ammonia is slowly added to adjust pH of solution to 9.5-10.5. The solution is isoelectric-deposited for 6-10 hours, centrifuged, precipitated, and precipitate, supernatant and mother liquor are collected. The precipitate is stirred in 95% alcohol, washed, centrifuged, precipitated and dried, to obtain L-arginine. The supernatant is vacuum distillated, and alcohol is recovered. The supernatant is mixed, to obtain supernatant. The mother liquor is extracted, concentrated, and pH is adjusted to 9.5-10.5. The L-arginine and mother liquor are extracted. Sulfuric acid is added to mother liquor and pH is adjusted to 7. The potassium humate with content of 2 %mass with respect to liquor is added to liquor, stirred, evaporated and spray-granulated, to obtain potassium sulfate as fertilizer.
NOVELTY - Municipal waste and combustible domestic waste are screened, and resultant waste is dried. The resultant material is crushed, and mixed with biodiesel, activated carbon, charcoal and paraffin mixture. The obtained product is extruded by an extruder and dried to obtain solid fuel.    USE - Manufacture of solid fuel (claimed).    ADVANTAGE - The method efficiently provides solid fuel using municipal waste.
NOVELTY - This utility model claims a biomass anaerobic fermentation stirring and heating system, belonging to the technical field of biomass anaerobic fermentation. By the anaerobic fermentation to generate marsh gas and air by a membrane separator to carry out physical separation to generate oxygen-enriched combustion needed by CH4 volume concentration of a combustible gas, oxygen-enriched and a CO2-rich gas, oxygen-enriched combustion generating gas-liquid two phase jet flow required to heat water, gas-liquid two phase jet flow of the hot water enters the jet nozzle to accelerate, the liquid phase jet flow suction effect the CO2-enriched gas suction nozzle to form a gas-liquid jet. The track gas-liquid two phase jet flow device is installed in the anaerobic fermentation tank to move to form a moving and swinging of the gas-liquid two phase jet flow. This utility model through the movement regulation of gas-liquid two-phase jet device, the global fermentation raw material stirring and heating the fermentation tank, strengthening anaerobic fermentation tank, heat exchange and mass exchange of the fermentation material.
NOVELTY - The high-efficiency film reactor a hollow fibrous membrane component, mainly composed of a biochemical aeration tank, a hollow fibre membrane component, the water guide section and a guide baffle plate, wherein, is provided with a horizontal water inlet at the bottom of the biochemical aeration tank and the bottom water discharging port, the tank is set with a group of efficient turbulent flow aerator, the bottom of the guide area is set with guide plate, the guide vertically installed in the water region is provided with an aeration supporting pipe of the hollow fibre membrane component. Biochemical aeration tank is installed below the efficient turbulence aerator the active sludge in the pool, the guide water inlet reflowing the active sludge and sewage mixing water inlet, which can effectively reduce the large particles and the water flow impact of a damage to a component, which greatly reduces the hollow fibre membrane to separate. Compared with the existing technology, the high efficiency of the membrane bioreactor is not only good water quality, pollution-resistant performance and anti-impact performance, small floor area and the system without discharging residual sludge.
NOVELTY - A system comprises methanation unit comprising catalyst in which synthesis gas is converted to crude synthesized natural gas, carbon dioxide and sulfide gas removal unit in which carbon dioxide and sulfide gas in crude synthesized natural gas is removed, supplementary methanation reactor unit in which carbon dioxide, carbon monoxide and hydrogen in the crude synthesized natural gas are converted to methane and water, to obtain synthesis gas and dehydration unit in which water in synthesis gas is removed, to obtain methane-enriched synthesis gas.    USE - System used for manufacturing methane-enriched synthesis gas (claimed).    DETAILED DESCRIPTION - A system comprises methanation unit comprising catalyst in which synthesis gas is converted to crude synthesized natural gas comprising methane, carbon dioxide, carbon monoxide, hydrogen and sulfide gas by direct methanation reaction, carbon dioxide and sulfide gas removal unit in which carbon dioxide and sulfide gas in crude synthesized natural gas is removed such that concentration of sulfide gas is less than 5 ppm, supplementary methanation reactor unit in which carbon dioxide, carbon monoxide and hydrogen in the crude synthesized natural gas are converted to methane and water by supplementary and direct methanation reaction using catalyst (A), to obtain synthesis gas and dehydration unit in which water in synthesis gas is removed, to obtain methane-enriched synthesis gas. The catalyst (A) is sulfur-resistant direct methanation catalyst and sulfide gas concentration is less than 5 ppm.
NOVELTY - Low temperature marsh gas accelerator comprises iron salt, cobalt salt, nickel salt, and yeast powder in a ratio of 3:1-2:1-2:1-2.    USE - Used as a low temperature marsh gas accelerator.    ADVANTAGE - The accelerator is provided with simple composition; is economical and easy to prepare, and convenient and quick to use; can realize the low temperature and high-efficient marsh gas production; can greatly reduce labor cost; and can satisfy the production requirement of all scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing low temperature marsh gas accelerator, comprising placing the iron salt, cobalt salt or nickel salt into the container, adding distilled water to prepare saturated solution, then adding yeast powder, stirring and mixing uniformly to obtain the low temperature marsh gas accelerator.
NOVELTY - Disclosed is a continuous process to manufacture Hexa-Chloro Ethane from lower chlorinated ethylene (Per chloro Ethylene) using Solar energy. The process provides instant chlorination due to the reaction setup to form Hexa-Chloroethane. The said process helps in making the final product moisture free, economical and safer to use be used in Aluminium smelter plants.
NOVELTY - A composite nanomaterial comprises copper selenide nanobelt loaded with nickel nanoparticles.    USE - Composite nanomaterial is used for hydrogen evolution reaction.    ADVANTAGE - The composite nanomaterial, when compared with a molybdenum disulfide/graphene composite hydrogen evolution reaction catalyst, uses a structure in which nickel nanoparticles are distributed on cobalt selenide nanobelt. The nickel nanoparticles are compactly arranged, and have high conductivity, such that the resistance of composite material is reduced. With the cobalt selenide nanobelt structure, enough active catalytic sites are provided for reaction. The cobalt selenide nanobelt has excellent hydrogen evolution reaction catalytic activity. The nanobelt and nanoparticles provide a synergistic effect, such that the catalytic activity of the composite nanomaterial is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite nanomaterial, which involves mixing cobalt salt, sodium selenite, and amine solvent with water, heat-reacting the mixture to obtain cobalt selenide nanobelt, mixing the nanobelt with nickel and solvent, and heat-reacting.
NOVELTY - A black liquid straw carbon is obtained by mixing straw and paper pulping black liquor as raw material, molding and carbonizing.    USE - Black liquor straw carbon (claimed).    ADVANTAGE - The black liquid straw carbon is environmentally-friendly, and efficiently and economically prepared with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of black liquid straw carbon.
NOVELTY - Preparation of biodiesel involves preparing peracid value rice bran oil and carbinol as raw materials, carrying out interesterification reaction of triglyceride and the carbinol, carrying out esterification reaction of fatty acid and the carbinol, conducting interesterification reaction and the esterification reaction in reactor. The peracid value rice bran oil contains free fatty acid and triglyceride.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The biodiesel is economically prepared with high reaction speed and transformation rate without polluting the environment, by simple method.
NOVELTY - The system has a modifier (1) that is provided with a modification catalyst (2) which modifies the hydrogen type fuel and generates hydrogen. A heat exchanger (5) which is positioned more downstream than the modifier heat-exchanges between the reformed gases produced by reformation of the mixed gas. A regenerator (21) is provided to thermally store the heat moved by the heat exchanger from the reformed gas. A catalyst temperature raising unit accelerated the temperature rising of an oxidation catalyst (3) using the heat thermally stored by the regenerator.    USE - Reformation system for supplying hydrogen to air-intake system of internal combustion engine.    ADVANTAGE - The shortening of the arrival time to the reformation temperature of the modification catalyst is attained by carrying out structure arrangement of the regenerator which receives and thermally stores supply of the heat moved by the heat exchanger from hot reformed gas. Hence the power consumption of the reformation system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the reformation system. (Drawing includes non-English language text)    Modifier (1)    Modification catalyst (2)    Oxidation catalyst (3)    Heat exchanger (5)    Regenerator (21)
NOVELTY - Sludge with water content of 75-90%, is injected into a reaction kettle, and saturated steam is injected with the pressure of 1.5-2.5 MPa into thermal hydrolysis reactor. The injection of saturated steam is terminated when the temperature of the sludge reaches 150-185 degrees C, and maintained for 0-25 minutes, to obtain slurry which is subjected to thermal hydrolysis. The resultant slurry is subjected to anaerobic digestion reaction to obtain marsh gas.    USE - Method for treatment and utilization of sludge based on thermal hydrolysis for forming marsh gas used as fuel for steam boiler system.    ADVANTAGE - The thermal hydrolysis treatment temperature is low, so that the time for heating the sludge and total treatment time during the treatment process is shortened. The method efficiently and economically treats the sludge based on thermal hydrolysis with high recycling property, with reduced consumption of energy without affecting the environment.
NOVELTY - Wastewater containing acidic organic component and scale component is supplied to methane fermentation tank via pH control unit, and anaerobic wastewater treatment is carried. At least 2 points of pH(a1) and pH(a2) are set as target pH in pH control unit, and pH(t1) and pH(t2) are set as setting pH of effluent. When pH of effluent from fermentation tank is less than pH(t1) and pH of effluent is more than pH(t2), target pH in pH control unit is set to pH(a2). An acid and/or an alkali are added to pH control unit, and pH of influent to methane fermentation tank is adjusted.    USE - Anaerobic treatment of wastewater e.g. whiskey distillation residual liquor, shochu-liquor distillation residual liquor, sugar manufacturing wastewater and starch wastewater.    ADVANTAGE - The wastewater is stably and efficiently treated. The precipitation of scale component is suppressed.    DETAILED DESCRIPTION - Wastewater containing an acidic organic component and a scale component, which precipitates in an alkaline region is supplied to methane fermentation tank via a pH control unit, and anaerobic wastewater treatment is carried. At least 2 points of pH(a1) and pH(a2) are set as target pH in pH control unit, and pH(t1) and pH(t2) (pHt1 less than or equal to pHt2) are set as setting pH of the effluent from fermentation tank. When pH of the effluent from fermentation tank is less than pH(t1) and pH of the effluent is more than pH(t2), target pH in pH control unit is set to pH(a2). An acid and/or an alkali are added to pH control unit, and pH of the influent to methane fermentation tank is adjusted such that target pH in pH control unit is set to pH(a1). An INDEPENDENT CLAIM is included for anaerobic wastewater treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow sheet explaining treatment of wastewater. (Drawing includes non-English language text)
NOVELTY - A (1E,4E)-1-phenyl-5-(2,6,6-trimethylcyclohex-1-en-1-yl)penta-1,4-dien-3-one compound (I) is new.    USE - New (1E,4E)-1-phenyl-5-(2,6,6-trimethylcyclohex-1-en-1-yl)penta-1,4-dien-3-one compound is used as lure for attracting Adelphocoris suturalis Jakovlev and Apolygus lucorum Meyer-Dur.    ADVANTAGE - The 1E,4E-1-phenyl-5-2,6,6-trimethylcyclohex-1-en-1-yl-penta-1,4-dien-3-one compound is prepared by simple, efficient, economical and environmentally-friendly method.    DETAILED DESCRIPTION - A (1E,4E)-1-phenyl-5-(2,6,6-trimethylcyclohex-1-en-1-yl)penta-1,4-dien-3-one compound of formula (I) is new.    R=4-H, 4-F, 4-Cl, 4-Br, 4-CH3, 4-CH2CH3, 4-0CH3, 4-0CH2CH3, 4-N02, 3-CH3, 2-0CH3, 3,4-(CH3)2 or 3,4-Cl2.
NOVELTY - Preparation of 5-hydroxymethylfurfural involves using biomass sugar as raw material, acid and chloride as combined catalyst, carrying out one-pot method in a solution of water and dimethyl sulfoxide, hydrolyzing resultant product, isomerizing, neutralizing the resultant product, dehydrating, separating resultant product and drying.    USE - Preparation of 5-hydroxymethylfurfural (claimed).    ADVANTAGE - The 5-hydroxymethylfurfural is economically and environmentally-friendly manufactured with high yield, by simple process.
NOVELTY - A biogas purifying system comprises first stage inlet separator for granular solid material and water to form purifying marsh gas, first stage compressor for compressing first purifying marsh gas to form compressed gas, compressor for compressing the first compressed gas to form compressed gas, inlet separator, purified marsh gas washing tower for removing amine liquid in second purifying marsh gas, and liquid circulation device for removing absorbed impurity gas in amine solution and recycling the amine solution to the washing tower.    USE - Biogas purifying system.    ADVANTAGE - The system is capable of increasing marsh gas methane content.    DETAILED DESCRIPTION - Biogas purifying system comprises first stage inlet separator for granular solid material and water to form purifying marsh gas, first stage compressor connected with the first stage inlet separator for compressing the first purifying marsh gas to form compressed gas, compressor connected with the first stage compressor for compressing the first compressed gas to form compressed gas, inlet separator connected with secondary compressor, purified marsh gas washing tower connected with secondary inlet separator for removing amine liquid in second purifying marsh gas, and liquid circulation device connected with the washing tower for removing absorbed impurity gas in amine solution and recycling the amine solution to the washing tower.
NOVELTY - A biogas purifying system comprises first grade inlet separator for granular solid material and water in marsh gas, compressor for compressing first purifying marsh gas to form compressed gas, secondary compressor for compressing first compressed gas to form compressed gas, secondary separator inlet for removing second compression in the marsh gas for particulate solid material and water to form purifying marsh gas, and purifying device for removing second purifying marsh gas in carbon monoxide and water to obtain purified marsh gas.    USE - Biogas purifying system.    ADVANTAGE - The system improves content of methane in marsh gas.    DETAILED DESCRIPTION - Biogas purifying system comprises first grade inlet separator for granular solid material and water in marsh gas, compressor connected with first grade inlet separator for compressing first purifying marsh gas to form compressed gas, secondary compressor connected with first grade compressor for compressing first compressed gas to form compressed gas, secondary separator inlet connected with secondary compressor for removing second compression in the marsh gas for particulate solid material and water to form purifying marsh gas, and purifying device connected with secondary inlet separator for removing the second purifying marsh gas in carbon monoxide and water to obtain purified marsh gas.
NOVELTY - An organic waste is supplied to dryer and fermenter. The dryer comprises kiln dryer and paddle dryer. The hydrocarbons in organic waste are passed through kiln dryer for carbonized fuel production.    USE - Method of processing organic waste used for producing carbonized fuel and fertilizer (all claimed).
NOVELTY - The system has an oxygen storage tank (49) that is configured to store oxygen generated in an anode (42). A condenser is configured to separate the second mixer including the hydrogen generated in a cathode (41). A high temperature steam electrolysis stack (43) is configured to produce hydrogen and oxygen. A high temperature steam electrolysis stack is configured to use generated waste and is moved to mixed gas inlet port and produced hydrogen is transferred and stored in a hydrogen storage tank (50).    USE - Hydrogen production system used in nuclear power plant.    ADVANTAGE - The waste heat ejected from fuel cell generation system is utilized for the high temperature steam electrolysis and the efficiency of the hydrogen production system can be improved. The nuclear power generation can be used as the power source for the system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen production system.    Cathode (41)    Anode (42)    High temperature steam electrolysis stack (43)    Oxygen storage tank (49)    Hydrogen storage tank (50)
NOVELTY - An isomerization catalyst contains 0.01-5 wt.% group VIII noble metal element, 10-80 wt.% rare-earth modified mordenite, 0.1-10 wt.% auxiliary agent, and balance halogen-containing binder of 0.5-5 wt.% in which rare-earth modified mordenite based on amount of rare-earth metal oxide which is 5-40 wt.%.    USE - An isomerization catalyst (claimed).    ADVANTAGE - Product has improved activity, stability, performance, and dispersion degree of noble metal component due to addition of auxiliary agent, reduces load of active metal component, and is low cost.
NOVELTY - Producing fuel ethanol, comprises: (1) pre-treating a fiber raw material and a cheap carbon source raw material; (2) mixing the pretreated fiber raw material and the pretreated cheap carbon source raw material and carrying out pre-enzymatic hydrolysis; and (3) selectively adding a fermentable sugar raw material in the fiber raw material having undergone pre-enzymatic hydrolysis, adjusting temperature, adding Saccharomyces cerevisiae and carrying out synchronous saccharification and joint fermentation for production of ethanol.    USE - The method is useful for producing fuel ethanol (claimed).    ADVANTAGE - The method can effectively increase the concentration of ethanol in the fermentation broth of the fiber raw material and reduce energy consumption in the phase of concentration of ethanol and has the advantages of simple production flow and high ethanol yield.    DETAILED DESCRIPTION - Producing fuel ethanol, comprises: (1) pre-treating a fiber raw material and a cheap carbon source raw material; (2) mixing the pretreated fiber raw material and the pretreated cheap carbon source raw material and carrying out pre-enzymatic hydrolysis, where a weight ratio of the cheap carbon source raw material to the fiber raw material is 1:3-3:1 on a dry basis, an obligate hydrolase preparation is used in the process of pre-enzymatic hydrolysis, and the obligate hydrolase preparation contains cellulase and comprises diastase and/or inulase at the same time; and (3) selectively adding a fermentable sugar raw material in the fiber raw material having undergone pre-enzymatic hydrolysis, adjusting temperature to 24-44 degrees C, adding Saccharomyces cerevisiae and carrying out synchronous saccharification and joint fermentation for production of ethanol.
NOVELTY - Distiller's grains alkaline hydrolysis liquid glucose solution is claimed. The distiller's grains alkaline hydrolysis liquid glucose is rich in minerals and salts.    USE - The distiller's grains alkaline hydrolysis liquid glucose solution is useful for producing ethanol fuel (claimed).    ADVANTAGE - In method, by-product hydrolysis residue can be used as an adsorbent material, and condensate and a residue can be reused.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned distiller's grains alkaline hydrolysis liquid glucose solution, which involves subjecting raw materials containing distiller's grains to blending, hydrolysis by microwave heating at 50-160 degrees C for 0.5-3 hours, liquid slag separation, concentration (under reduced pressure) and pH regulation (to 4-5 using hydrochloric acid, phosphoric acid, sulfuric acid, sulfurous acid and nitric acid), where alkaline catalysis, and vacuum distillation are performed.
NOVELTY - Distillers' grains acid hydrolysis liquid glucose used for producing and fermentation of fuel ethanol.    USE - The distillers' grains acid hydrolysis liquid glucose used for producing and fermentation of fuel ethanol (claimed).    ADVANTAGE - The process's by-product hydrolysis residue can be used as an adsorbent material; a condensate and a lotion can be reused; and the prepared distillers' grains acid hydrolysis liquid glucose contains a certain amount of minerals and salts, and can be directly used for production of ethanol fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of preparing distillers' grains acid hydrolysis liquid glucose, comprising subjecting raw materials containing distiller's grains to blending, hydrolysis by microwave heating, liquid slag separation, concentration, and pH regulation.
NOVELTY - Kitchen waste biogas liquid processing method comprises performing kitchen garbage biogas coagulation and sedimentation in sedimentation tank, introducing the biogas slurry into anoxic tank, carrying out denitrification reaction in the anoxic tank, conducting nitration reaction in aerobic tank, processing biogas slurry in membrane bioreactor (MBR) for sludge-water separation.    USE - Method for processing kitchen garbage biogas liquid.    ADVANTAGE - The method has low energy consumption, high degree of automation, and full automatic operation, saves human resource, has no harm to human body, has no secondary pollution to environment, is provided with cover plate and matched odor collecting processing system for odor control, can absorb fan shock and realizes noise insulation.    DESCRIPTION OF DRAWING(S) - The drawing is a block diagram of kitchen waste biogas liquid processing method (Drawing includes non-English language text).
NOVELTY - Research and development and industrialization of microbial ecological organic fertilizer comprises selection of a series of strain with high efficiency and high quality, researching the mechanism of action of functional microorganisms i.e. Azotobacter, phosphorus-solubilizing bacteria, and potassium-solubilizing bacteria, researching the microecological chemical compound according to different kinds of fermentation materials, and designing a series of different strain by microbial agent.    USE - Research and development and industrialization of microbial ecological organic fertilizer (claimed) used for improving soil physicochemical property, enhancing soil holding water, improving soil fertility, providing nutrition for crops, inhibiting the growth and spreading of pathogenic microorganism, improving crop rhizosphere environment, and reducing the occurrence of diseases of crops.    ADVANTAGE - Waste produced by organic vegetable production is subjected to microbial fermentation and then fully used as an organic vegetable fertilizer. The organic vegetable fertilizer greatly improves crop yield and crop quality.
NOVELTY - Biomass raw material is boiled in an organic acid formed by formic acid and acetic acid in presence of hydroxide peroxide as catalyst, and reaction temperature is controlled at 90-120 degrees C for 10-90 minutes to obtain sugar solution. Obtained sugar solution is subjected to dehydration reaction, and subsequently solid-liquid separation is carried out on obtained liquid, such that solid-liquid mass ratio is 1:5-1:20. Mass ratio of acetic acid and formic acid is 1:19-19:1. The obtained reaction mixture is further rectified to obtain finished furfural. Biochar is obtained as byproduct.    USE - Manufacture of furfural (claimed).    ADVANTAGE - The method efficiently and economically provides furfural with reduced energy consumption, without affecting the environment.
NOVELTY - A Pantoea ananatis P21 strain, preservation number is CGMCC No. 5749, is new.    USE - The P. ananatis P21 strain is useful for producing a microbial agent used for preventing and treating crop diseases, where the diseases of crops are nematode disease, blight and/or powdery mildew (all claimed).    ADVANTAGE - The widely-applicable efficient phosphate solubilizing bacteria P. ananatis P21 and fungi for efficiently preventing nematodiasis are organically combined; and by utilizing the composite agent, the soil phosphorus is efficiently used, the utilization rate of phosphate fertilizer is improved, the function of microorganism in preventing nematodiasis is sufficiently realized, and an effect of increasing yield by solubilizing phosphate and preventing diseases is realized, thus having great significance to sustainably increasing grain yield of the country, saving phosphate fertilizer resource, reducing nematodiasis and protecting the ecological environment of farmland.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a composite microbial agent, comprising P. ananatis P21 and Hirsutella minnesotensis as active ingredients.
NOVELTY - Strain of nodule bacteria Bradyrhizobium japonicum 859 (VNIISHM No.24117) is proposed, used as a facility to produce a fertiliser for soya. When soya seeds are treated with the fertiliser produced on the basis of the specified strain Bradyrhizobium japonicum, the index of germination increases by more than 8%, and crop capacity increases by 17-30%.    USE - Biotechnologies.    ADVANTAGE - Higher germination of plants, improved crop capacity.4 tbl
NOVELTY - Preparation of methane comprises performing microalgae and anaerobic activated sludge mixed fermentation under anaerobic conditions; and collecting generated methane gas.    USE - Preparation of methane used as clean energy.    ADVANTAGE - The method adopts mixed fermentation of microalgae and anaerobic activated sludge, in which microbes in anaerobic activated sludge utilize proteins, sugars and lipid components in microalgal biomasses to carry out metabolism of anaerobic microbes, thus inorganic elements comprising nitrogen and phosphorus in microalgal biomasses can be effectively recovered and repeatedly utilized, while simultaneously generating methane gas.
NOVELTY - A biomass material thermal cracking furnace has hearth made of nickel alloy. The content of nickel alloy is 10-20 wt.%.    USE - Biomass material thermal cracking furnace is used for preparing natural gas (claimed) for producing methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of natural gas, which involves crushing the material, drying crushed material, delivering the dried material to a material storage plate in the furnace hearth, sweeping the material to the bottom of the furnace hearth, thermal cracking the material at 700 degrees C, obtaining gas state product, separating and cooling, obtaining combustible gas and liquid, compressing, and separating.
NOVELTY - A liquid fertilizer comprises 500-1000 pts. wt. stone powder, 10-20 pts. wt. cell wall bacteria, 15-50 pts. wt. honey, 15-50 pts. wt. brown sugar, 10-30 pts. wt. captan, 10-30 pts. wt. carbendazim, 10-30 pts. wt. triphenyltin acetate, 10-30 pts. wt. antifungal, 10-20 pts. wt. cypermethrin, 10-20 pts. wt. fipronil, 10-30 pts. wt. acetamiprid, 10-30 pts. wt. alum, 10-20 pts. wt. calcium superphosphate, 5-20 pts. wt. potassium sulfate, 5-20 pts. wt. potassium dihydrogen phosphate, 5-20 pts. wt. zinc sulfate, 5-20 pts. wt. manganese sulfate, and 3-20 pts. wt. borax.    USE - Liquid fertilizer used for beet planting (claimed).    ADVANTAGE - The fertilizer improves sugar content of beet by 1-3%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of liquid fertilizer by adding stone powder, cell wall bacteria, honey, brown sugar, captan, thiram, carbendazim, triphenyltin acetate, antifungal, cypermethrin, fipronil, pyrethrin emulsifiable concentrate, fenvalerate, acetamiprid, and alum with 1-2 times amount of water in fermentation tank, stirring at 25-35 degrees C, fermenting for 7-10 days to obtain fermentation broth, extracting in secondary fermentation tank, adding 2-3 times amount water, and fermenting while stirring twice daily at 25-35 degrees C for 7 days to obtain second fermentation broth; mixing calcium superphosphate, potassium sulfate, potassium dihydrogen phosphate, zinc sulfate, manganese sulfate, and borax with water at ratio of 1:8-1:10 in container, dissolving in hot water, and stirring twice daily for 3 days to obtain dissolved inorganic salt solution; and adding with second fermentation broth, and stirring.
NOVELTY - The biological treatment apparatus has an anaerobic reaction tank (7) that processes an alkaline organic waste-water on anaerobic conditions. A ventilation unit ventilates portion of the biogas emitted in the anaerobic reaction tank to the alkaline organic waste-water. A natural water tank (2) accepts the alkaline organic waste-water. A blower (9) supplies the biogas from the anaerobic reaction tank to diffusion tube. A piping (8) guides a portion of biogas flowing out of the natural water tank to the inlet side of blower.    USE - Biological treatment apparatus of alkaline organic waste-water.    ADVANTAGE - The acidic substances such as carbon dioxide, and hydrogen sulfide in biogas, and dissolved in alkaline organic waste-water can be removed from gas. The required amount of an acid for neutralization of alkaline organic waste-water can be reduced and the load of gas treatment installation can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological treatment apparatus. (Drawing includes non-English language text)    Natural water tank (2)    Hanging wall (2a)    Anaerobic reaction tank (7)    Piping (8)    Blower (9)
NOVELTY - An emodin in Polygonum is separated and purified by drying Polygonum, crushing, extracting through refluxing with ethanol, filtering, concentrating, separating through macro-porous resin, washing with water, eluting with ethanol, decompressing, concentrating, recovering ethanol, and purifying emodin through silica gel column chromatography.    USE - Separation and purification of emodin in Polygonum (claimed).    ADVANTAGE - Product has high purity. Preparation process is simple, low-cost, and non-polluting.
NOVELTY - (7-methoxy-1-naphthyl)ethylamine is synthesized by reducing (7-methoxy-1-naphthyl)acetamide with hydrogen-containing siloxane-metal activator in reducing system to form (7-methoxy-1-naphthyl)ethylamine or its acid salt.    USE - Synthesis of (7-methoxy-1-naphthyl)ethylamine for synthesizing agomelatine (claimed).    ADVANTAGE - Synthesis of (7-methoxy-1-naphthyl)ethylamine for synthesizing agomelatine is environment-friendly, has mild reaction conditions, high yield, good selectivity, and metal complexes that are cheap and easy to obtain, and does not require high-pressure hydrogenation equipment.    DETAILED DESCRIPTION - (7-methoxy-1-naphthyl)ethylamine of formula (I) is synthesized by reducing (7-methoxy-1-naphthyl)acetamide of formula (II) in hydrogen-containing siloxane-metal activator reducing system to form (7-methoxy-1-naphthyl)ethylamine or its acid salt. . An INDEPENDENT CLAIM is included for synthesis of agomelatine which involves coupling (7-methoxy-1-naphthyl)ethylamine or its acid salt with acetic anhydride or acetyl chloride.
NOVELTY - A deoxynojirimycin frosted mulberry leaf is extracted by cleaning frosted mulberry leaf, cutting, drying, covering with packing food-level plastic film, piling, fermenting at 30-50 degrees C until mycelia grow from all leaves, drying at less than or equal to 65 degrees C, loading into cloth bag, soaking, extracting through extracting device according to combination of ultrasonic waves and microwaves.    USE - Extraction of deoxynojirimycin from frosted mulberry leaf (claimed).    ADVANTAGE - Preparation process is simple, low-cost, and non-polluting due to absence of organic solvents.
NOVELTY - A carbonyl group-containing compounds (III) or (IV) as raw material is reacted under the action of the strong alkali hypohalite and oxidizing agent, to obtain key intermediate 17-beta-carboxylic acid derivative of fluticasone compounds (I) or (II).    USE - Synthesis of key intermediate 17-beta-carboxylic acid derivative of fluticasone (claimed).    ADVANTAGE - The key intermediate 17-beta-carboxylic acid derivative of fluticasone is efficiently prepared with excellent selectivity, and high yield without polluting the environment, by a simple method.    DETAILED DESCRIPTION - A carbonyl group-containing compounds of formula (III) or (IV) as raw material is reacted under the action of the strong alkali hypohalite and oxidizing agent, to obtain key intermediate 17-beta-carboxylic acid derivative of fluticasone compounds of formula (I) or (II).    R1,R5=H or halo;    R2,R3=H, OH or halo chosen from F, Cl, Br and I;and    R4,R6=H, OH or 1-4C linear alkyl.
NOVELTY - Decarboxylation reaction of carboxyl group-containing compound (II) is carried out in presence of monovalent metal silver salt catalyst and selective fluorinating reagent, to obtain fluticasone derivative (I).    USE - Synthesis method of fluticasone derivative (claimed).    ADVANTAGE - The method enables economical synthesis of nontoxic fluticasone derivative with high selectivity and yield by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Decarboxylation reaction of carboxyl group-containing compound of formula (II) is carried out in presence of monovalent metal silver salt catalyst and selective fluorinating reagent, to obtain fluticasone derivative of formula (I). The selective fluorinating reagent contains fluoro group-containing compound of formula (III).    R=C2H5CO- or C4H3O-CO-;and    X=BF4. PF6 or CF3SO3.
NOVELTY - Invention relates to public utilities and environmental biotechnology and can be used for bioconversion of sewage sludge with low content of heavy metals combined with brewery wastes - spent grains - into compost. The method involves mixing in a defined volume ratio dry sewage sludge with an organic component in form of spent grains and with a cellulose-containing component in form of saw dust, adding a compost ferment in amount of at least 15% of the volume of the mixture and subsequent aerobic composting of the mixture. After the high-temperature composting step, natural drying of the mixture which is placed in a layer of about one metre, is carried out while simultaneously adding a bioactivator in form of a liquid culture containing 109-1010 cells per ml of a suspension of anoxic purple phototrophic bacteria Rhodobacter capsulatus in volume ratio to the mixture of at least 1:50, respectively, and holding without compulsory aeration for 25-30 days, followed by stabilisation of the mixture in piles for 30-35 days.    USE - Chemistry.    ADVANTAGE - Inventions accelerates maturation and improves the quality of the compost by activating microbial succession and enhancing anti-fungal properties of the compost, improved sanitary-bacteriological and agrochemical properties, low cost of the end product.5 tbl, 5 ex
NOVELTY - The briquette structure has a frame for accommodating red clay and water. The red clay and water are mixed, to obtain the hardwood charcoal powder. The cylindrical bore coal (1) is compressed. A circular hole (5) is formed in the cylindrical upper side (3) having specific diameter. The hardwood charcoal and main coal are perpendicularly passed through hole. The vertical fin is adhered in lower base of frame. The hardwood charcoal and main coal are mingled with compressed cylindrical bore coal and are combusted to efficiently roast the meat using combustion flame.    USE - Holed briquette structure of hardwood charcoal and coal used in restaurant and outdoor used for roasting meat, boned rib and boston butt.    ADVANTAGE - The red coal and water can be mixed together so as to obtain the hardwood charcoal powder. The cylindrical bore coal can be compressed easily. The hardwood charcoal consumption rate can be reduced. The oak consumption rate can be reduced. The environmental protection effect can be improved. The generation of harmful chemical species during the combustion of hardwood charcoal and coal is prevented, such that the health of user is not affected. The commercial briquette structure height is decreased. The heat can be generated easily and quickly and the meat can be roasted efficiently. The charcoal burning time can be reduced. The people prefer to use the briquette structure. The preference of the people for the product can be improved. The calorie level of the meat can be reduced, by roasting the meat using the combined hardwood charcoal and coal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the holed briquette structure.    Cylindrical bore coal (1)    Cylindrical upper side (3)    Circular hole (5)    Hardwood charcoal layer (8)    Coal seam (9)
NOVELTY - The method involves assembling rotary die and cartridge die to guide jig. A roller shield spindle is rotated using planetary gear. The shaft is rotated to another-axis. The cartridge die is adhered to front cover. The air gun and air driver are arranged in housing.    USE - Method for recycling domestic waste.    ADVANTAGE - The assembly time is shortened and the cleaning efficiency is improved. The domestic waste can be processed and recycled efficiently.
NOVELTY - Method for extracting oleanolic and ursolic acid from pawpaw, involves drying fresh pawpaw and crushing to obtain the powder, extracting the powder, filtering and separating the extracting liquid, repeating the extracting process for 2-3 times, combining the extracting solution, filtering the supernatant, absorbing the supernatant on macroporous absorption resin column, using 5-10 times of water, eluting the extract and then using 20-80% of ethanol water solution, collecting the eluate, and concentrating and drying the product.    USE - The method is useful for extracting oleanolic and ursolic acid from pawpaw (claimed).    ADVANTAGE - The extraction method does not need any special device, and is rapid, simple, nontoxic and environmentally-friendly.
NOVELTY - Solvent-based gas hydrate coupling enhancer comprises gas solvent and hydrate promoter at a ratio of 21:1 to 1:6. The gas solvent is sulfolane or dimethyl sulfoxide. The hydrate promoter is alkyl compound (I) or pyrrole compound (II).    USE - Solvent-based gas hydrate coupling enhancer used for gas purification, and for storing and transporting gas hydrate (claimed). It can be widely applied to hydrate gas separation, hydrate seawater desalination and energy application.    ADVANTAGE - The gas hydrate coupling enhancer is water-soluble, promotes gas dissolution, and can make gas hydrate generating pressure of 90% at the same temperature. The hydrate reaction rate is 146%, and the gas hydrate has storage capacity of 162 v/v for 2-3 hours, which can greatly shorten the gas storage and transportation process of the operation time, reduce equipment and save cost.    DETAILED DESCRIPTION - Solvent-based gas hydrate coupling enhancer comprises gas solvent and hydrate promoter at a ratio of 21:1 to 1:6. The gas solvent is sulfolane or dimethyl sulfoxide. The hydrate promoter is alkyl compound of formula R2-R+(R1)(R3)-R4.X- (I) or pyrrole compound of formula (II).    R=N or P;    R1-R4=1-6C alkyl;    X=Be, F, Cl, NO3;    R5=O or C; and    R6-R9=H or 1-3C alkyl.
NOVELTY - Synthesis of beta -enaminone comprises reacting ketone derivative and aromatic nitrile derivative in the presence of copper catalyst to synthesize a series of beta -enaminone compound. The ketone is aromatic ketone, heterocyclic ketone and aliphatic ketone.    USE - Method for synthesizing beta -enaminone used in pharmaceuticals (claimed).    ADVANTAGE - The method has less reaction steps, inexpensive catalyst and mild reaction and is environment-friendly.    DETAILED DESCRIPTION - Synthesis of beta -enaminone derivative of formula (I) comprises reacting ketone derivative of formula (II) and aromatic nitrile derivative of formula (III) in the presence of copper catalyst to synthesize a series of beta -enaminone compound. The ketone is aromatic ketone, heterocyclic ketone and aliphatic ketone.    R1=ortho-, meta- or para- C6H6, thiophene, cyclohexyl or alkyl;    R2=H, alkyl, nitrile, aromatic nitrile or heterocyclic nitrile; and    R3=ortho-, meta- or para- C6H6 or heterocyclic.    An INDEPENDENT CLAIM is included for the preparation of beta -enaminone comprising:    (A) adding copper catalyst and base to Schlenk flask, vacuumizing at 3-15 torr, adding ketone, aromatic nitrile and organic solvent, placing in oil bath under nitrogen protection, reacting at 80-200 degrees C for 12-48 hours, where molar ratio of ketone to copper catalyst is 1:0.01-0.5 and aromatic nitrile to copper catalyst is 1:1-1.3 and volume of organic solvent is 1-10 ml;    (B) controlling reaction to room temperature, adding water, extracting 3 times with ethyl acetate and combining organic phase;    (C) drying with anhydrous sodium sulfate for 1 hour and vacuumizing to 20 torr to remove organic solvent; and    (D) eluting with petroleum ether or ethyl acetate by silica gel column.
NOVELTY - A degradable fertilizer bag comprises a degradable bag main material, and a fertilizer contained in the degradable bag main material. The degradable bag main material comprises an inner layer, an outer layer, and a water-retaining agent layer formed between the inner layer and the outer layer.    USE - Degradable fertilizer bag (claimed).    ADVANTAGE - The degradable fertilizer bag has excellent usability, is economical and environmentally-friendly. The fertilizer can naturally degrade over a period of time. When the fertilizer is used, water is profoundly poured, the water-retaining agent can fully absorb the water to saturate, and then the fertilizer is directly embedded into the soil, and even if no rain falls and no irrigation or fertilization exist for three to four months, nutrients required by plants can be guaranteed by the fertilizer, and moisture required by the plants can be guaranteed by the moisture contained in the water-retaining agent.
NOVELTY - Extraction of organic fertilizer from garbage, comprises collecting from source, dividing household garbage into kitchen garbage, plastic and paper; crushing other kitchen garbage and waste from meat and vegetable, pumping into temporary storage pool, crushing waste and dead materials from feeding industry, and human wastewater treatment residue, and pumping to temporary storage pools; and using drive-in ozone-free sterile water toilet ZL200910144911.0 and ozone-free sterile water squatting pan, and mixing with collected human waste.    USE - Method for extracting organic fertilizer from garbage (claimed).    DETAILED DESCRIPTION - Extraction of organic fertilizer from garbage, comprises: (A) collecting from source, dividing household garbage into kitchen garbage, plastic and paper; (B) crushing other kitchen garbage and waste from meat and vegetable, pumping into temporary storage pool, crushing waste and dead materials from feeding industry, and human wastewater treatment residue, and pumping to temporary storage pools; and (C) using drive-in ozone-free sterile water toilet ZL200910144911.0 and ozone-free sterile water squatting pan, and mixing with collected human waste. Extraction of organic fertilizer from garbage comprises transparent sealed operation chamber (11) in working chamber (10), first and second electromagnet (16,17). The working chamber is provided with hopper (13) and auxiliary discharging device (26), motor (31), rotating drum (32,33), piston (40), thrust spring (41).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of extraction of organic fertilizer from garbage.    Working chamber (10)    Sealed operation chamber (11)    Hopper (13)    Electromagnet (16,17)    Auxiliary discharging device (26)    Motor (31)    Rotating drum (32,33)    Piston (40)    Thrust spring (41)
NOVELTY - A culture medium comprises 25-45 pts. wt. crab-flavored mushroom chaff, 10-20 pts. wt. wood chips, 20-35 pts. wt. cottonseed hulls, 10-20 pts. wt. corncobs, 8.0-12 pts. wt. wheat bran, 1.0-2.0 pts. wt. lime and 0.8-1.2 pts. wt. gypsum.    USE - Culture medium used for culturing oyster mushroom (claimed).    ADVANTAGE - The culture medium has rich nutrition necessary for mushroom growth, thus improving yield of oyster mushroom which has biological efficiency of 92-98%. The environment-friendly method reduces production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing method of oyster mushroom comprising:    (A) mixing crab-flavored mushroom chaff, wood chips, cottonseed hulls, corncobs, wheat bran, lime and gypsum to obtain mixture, adding water to water content of 55-65% and adjusting pH to 7.0-8.0 using lime to obtain culture medium;    (B) putting in sterile bag, putting in sterilizing pot for 2.8-3.2 hours, heating at 100 degrees C for 14-16 hours, stopping heating, high-pressure sterilizing at 116-124 degrees C for 3.5-4.5 hours, heating for 6-8 hours and naturally cooling to below 30 degrees C;    (C) inoculating using 5% inoculum, adding oyster mushroom, transferring to culturing room at 17-22 degrees C and humidity of 60-70%, culturing and fermenting for 35-45 days and checking quality and conditions; and    (D) managing mushroom fruiting to grow mycelium, controlling temperature at 20-26 degrees C, keeping temperature difference between day and night of 7-8 degrees C, ventilating at air relative humidity of 85-90% while controlling carbon dioxide concentration of less than 500 ppm and harvesting oyster mushroom.
NOVELTY - Preparing synthesis gas or hydrogen by direct connection of non-catalytic partial oxidation furnace with a British gas lurigi (BGL) gasifier (10-11) or a crushed coal pressurized slag gasifier, pressurized fixed bed gasifying to form a first crude gas, raw gas dust-removing directly or via pure oxygen, synchronizing oxygen non-catalytic partial oxidation reformer (20) with pure oxygen, injecting the oxygen into the non-catalytic partial oxidation reformer combustion, pyrolyzing the organic compound, and transforming to form a second crude gas.    USE - Method for preparing synthesis gas or hydrogen (claimed).    ADVANTAGE - The method can solve the problem of environmental pollution caused by the BGL gasification method, and can save environmental protection investment.    DETAILED DESCRIPTION - Preparing synthesis gas or hydrogen by direct connection of non-catalytic partial oxidation furnace with a BGL gasifier (10-11) or a crushed coal pressurized slag gasifier, where raw material is coal, pure oxygen as oxidant, and steam as gasification agent, pressurized fixed bed gasifying at 250-500 degrees C to form the first crude gas, raw gas dust-removing directly or via pure oxygen non-catalytic partial oxidation and transferring furnace, synchronizing oxygen non-catalytic partial oxidation reformer (20) with pure oxygen, injecting the compressed oxygen into the non-catalytic partial oxidation reformer combustion at above 1300 degrees C, pyrolyzing the organic compound at high temperature, and transforming at above 1300 degrees C to form a second crude gas. An INDEPENDENT CLAIM is included for a device for preparing synthesis gas or hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for preparing synthesis gas or hydrogen (Drawing includes non-English language text).    Gasifier (10-11)    Non-catalytic partial oxidation reformer (20)    Chilling washing device (30)    Water inlet (31)    Pure oxygen conveying pipe (52)
NOVELTY - Production of biodiesel comprises adding catalyst and methanol vapor to waste oil through liquid and gas phase inlet of venturi gas-liquid mixing ejector, mixing, carrying out esterification reaction at certain temperature, introducing esterified water and unreacted methanol to distillation column, discharging water at bottom of column, introducing methanol vapor at top of column to be circulated in venturi gas-liquid mixing ejector, circulating reaction liquid through circulation pump, immersing lower end of mixing ejector below liquid level of reaction liquid and ejecting liquid.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method is simple, has high reaction activity, high esterification rate and low energy consumption and uses small amount of methanol.
NOVELTY - Compost charging method, involves using wet sludge produced by sewage treatment plants as a raw material, mixing fermentation auxiliary materials and plasticizer with the raw material, stirring the obtained mixture to form stockpile, performing aerobic fermentation on the stockpile for at least 10 days, carrying out pile turning on the stockpile, decomposing the stockpile for at least 10 days, air-curing and packaging the obtained product.    USE - Compost charging method (claimed).    ADVANTAGE - The method has wide availability of raw materials, and is simple and cost-effective.
NOVELTY - The present invention relates to gas detection pre-treatment device and a method of testing gases. The gas detection pre-treatment device contains an inert gas cylinder, a standard gas cylinder, an untested gas cylinder, a separating unit, a first connecting tube, a cooling unit, and an interface unit. Each of the inert gas cylinder, the standard gas cylinder, and the untested gas cylinder has an outlet pipe connecting with the first connecting tube. The first connecting pipe couples with the separating unit, and the separating unit includes a controlling channel and a separation chamber. The control channel has a first control vale, a second control valve, and a third control valve. Inlet ends of the first control valve and the second control valve couple with the first connecting pipe, an outlet end of the second control valve connects with the interface unit, an outlet end of the third control valve connects with the interface unit, and the separation chamber is covered in the cooling unit. The present invention also provides a method of testing gases. The present invention can enhance testing safety and reliability.
NOVELTY - The apparatus has an outer container that surrounds an outer periphery of a rotary kiln furnace (2). A reflux gas supply pipe (20) is inserted into the furnace through a vent (5). A burner (3) is arranged at lower end of the furnace. The furnace is supported by a support roller (10). The steam from a steam supply pipe is supplied to the furnace. A steam emission hole (32) is formed at upper end of the furnace, to emit supplied steam on emission aperture of the reflux gas supply pipe.    USE - Apparatus for manufacturing bamboo activated carbon.    ADVANTAGE - The quality of bamboo activated charcoal can be improved effectively. The structural change of rotary kiln furnace can be reduced. The operating efficiency of manufacturing device can be improved. The activation reaction of charcoal can be accelerated. The flue gas can be emitted efficiently from furnace. The aqueous gasification of bamboo charcoal can be accelerated. The rapid micro pore can be formed in the manufacturing device. The manufacturing cost of charcoal can be reduced. The fuel consumption of manufacturing device can be reduced. The injection power of steam into furnace can be improved. The supply of excessive steam into furnace can be prevented. The supply quantity of steam into furnace can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the manufacturing device.    Rotary kiln furnace (2)    Burner (3)    Vent (5)    Support roller (10)    Reflux gas supply pipe (20)    Steam emission hole (32)
NOVELTY - The machine has a loading chamber (2) which is installed on a support frame. A hopper (2a) is formed in upper portion of loading chamber. A gear-box (22) is provided in outer side of loading chamber. A fixing hinge is adhered to vent (2b). A revolving cutter (7) is arranged for cutting extruded product. A driving hinge is adhered to the exterior of extrusion molding unit (4). A supporting apparatus is arranged for supporting heating extrusion molding unit in outer sidewall of loading chamber.    USE - Solid fuel extrusion machine of mixed refuse containing synthetic resin and paper.    ADVANTAGE - The installation and replacement of solid fuel extrusion machine can be carried out conveniently. The temperature of the extruded product can be maintained stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid fuel extrusion machine.    Loading chamber (2)    Hopper (2a)    Vent (2b)    Extrusion molding unit (4)    Revolving cutter (7)    Gear-box (22)
NOVELTY - A biological sludge preparing method involves concentrating excessive biological sludge from sewage plants to be more than 5 wt.%, and adding sodium hydroxide to sludge, and stirring. The mixture is neutralized with coal to coke water. The resulting suspension is separated by gravity to biological sludge with mohlman index less than 100 dm3 kg/m dry solids and liquid dispersible sediment with mohlman index greater than 100 dm3 kg/m dry solids. The precipitate with index less than 100 dm3/kg dry sludge is dewatered use as a component for coking coal blend.    USE - Method for preparation of biological sludge for use as coking coal blend component.    DETAILED DESCRIPTION - A biological sludge preparing method involves concentrating excessive biological sludge from sewage plants to be more than 5% of dry weight, and adding sodium hydroxide to 5-15 kg/1 m3 sludge, and stirring. The mixture is neutralized with coal to coke water at 20-40 degrees C and pH of 8-10. The resulting suspension is separated by gravity to biological sludge with mohlman index of less than 100 dm3 kg/m dry solids and liquid dispersible sediment with mohlman index of greater than 100 dm3 kg/m dry solids. The precipitate with index of less than 100 dm3/kg dry sludge is dewatered to more than 15 wt.%, as a component for coking coal blend.
NOVELTY - Dry sanitation product with concealed deposit composite used as health system for aqueous organic human waste, includes a tray to pickup excrete or urine, where the deposit is mixed with scent. A dispatcher is provided for mixing and drying the urine and excrete, where the deposit is transferred to ventilation unit.    USE - Dry sanitation product with concealed deposit composite used as health system for aqueous organic human waste.
NOVELTY - A waste activation sludge generated in aeration tank and settling tank is reacted with acid catalyst methanol by activated sludge process. The reactant is subjected to solid-liquid separation, to collect precipitated residual sludge. Fatty acid methyl ester is extracted from the liquid phase portion, and distilled, to collect methanol. The obtained methanol is feed to reacting waste activation sludge and acid catalyst methanol, and liquid phase portion including soluble sludge decomposition material is supplied to an aeration tank with an activated sludge process.    USE - Reduction method of residual sludge (claimed).    ADVANTAGE - The residual sludge is economically reduced with generation rate of 60%.
NOVELTY - Animal wastes are treated directly in animal farm facilities. A suspension of biomass of the Bacillus cereus 10.09.63 DEP strain deposited in the collection of the Russian State Centre for Quality and Standardisation of Veterinary Drugs and Feed is sprayed with number of healthy spore-forming bacteria Bacillus cereus of at least 2asterisk106 CFU/cm3, diluted with water in weight ratio of 1:60, respectively. The manure mass and manure effluent are collected and settled until separation into a liquid fraction and a solid fraction. After coagulation and clarification, the liquid fraction with pH not higher than 8.5 is used as biological fertiliser. The solid fraction is mixed with limed moss peat with pH not higher than 6.5 and coarse-grained sand with grain size of 1-3 mm with weight ratio of 1:(8-10):5. Soil with moisture content of not more than 65% is obtained.    USE - Chemistry.    ADVANTAGE - Invention simplifies recycling of animal wastes and enables to obtain biological fertiliser and soil.1 dwg, 5 tbl, 6 ex
NOVELTY - An ammonia removing method involves directing a quantity of liquid in which ammonia is dissolved in a stripping vessel that includes a drawer section, where the stripping vessel is a container for the liquid and has a pipe, followed by injecting a gas, preferably air, dispersing injected gas in the liquid phase, heating liquid phase at 40-80 degrees C, preferably 55-65 degrees C, removing gas from the pipe, where the removed gas comprises ammonia in the gaseous state.    USE - Method for removing ammonia from a liquid biogas plant and waste water.    ADVANTAGE - The method enables removing ammonia in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for removing ammonia.
NOVELTY - A large chicken farm waste is used to produce biogas by preprocessing chicken manure; performing fermentation at 35-38 degrees C with residence time of 20-25 days; and performing biological desulfurization technique to remove dihydrogen sulfide.    USE - Method for using large chicken farm waste to produce biogas (claimed).    ADVANTAGE - The method reduces waste pollution.
NOVELTY - Revaprazan is prepared by mixing guanidine salt, alkaline substance and 2-methyl ethyl acetoacetate; heating the mixture; adding halogenated reagent; heating the mixture; adding 1-methyl-1,2,3,4-tetrahydroisoquinoline; heating for electrophilic substitution reaction; adding acylating reagent; subjecting to acylation reaction; adding p-fluoro benzene and catalyst; and heating. The alkaline substance is sodium methoxide or sodium ethoxide. The catalyst is copper powder or cuprous chloride.    USE - Method of preparing a revaprazan (claimed).    ADVANTAGE - The method is easy and short, and has improved yield.
NOVELTY - Synthesis and purification of ceftiofur hydrochloride by adding organic solvent to reaction flask, adding cefuroxime acid, cooling, adding organic amine and S-2-benzothiazolyl 2-amino-alpha-(methoxyimino)-4-thiazolethiolacetate, stirring, and insulating to obtain solution; extracting and decolorizing aqueous phase with charcoal, filtering while stirring, adding hydrochloric acid to adjust the pH, precipitating solid, and filtering to obtain wet ceftiofur hydrochloride product; dissolving in acetone, adding hydrochloric acid to adjust the pH, slowly dropping water, crystallizing, standing, filtering, and drying to obtain ceftiofur hydrochloride.    USE - Synthesis and purification method of ceftiofur hydrochloride (claimed).    ADVANTAGE - The use of water as crystallizing solvent and reducing the use of organic solvent help to reduce production cost and environment pollution.    DETAILED DESCRIPTION - Synthesis and purification of ceftiofur hydrochloride by adding organic solvent to reaction flask, adding cefuroxime acid, cooling at 10 degrees C, adding organic amine and AE-active ester, uniformly stirring, and insulating at 10 degrees C for 3 hours to obtain solution; extracting with water and decolorizing aqueous phase with charcoal, filtering while stirring, adding 5 mol/L hydrochloric acid to adjust the pH value by 1-2, precipitating solid, and filtering to obtain wet ceftiofur hydrochloride product; dissolving in acetone, adding 5 mol/L hydrochloric acid to adjust the pH value by 1-1.4, slowly dropping water, crystallizing, standing for 2 hours, filtering, and drying at 40 degrees C to obtain ceftiofur hydrochloride.
NOVELTY - Simultaneous extraction of multiple active ingredients involves crushing bitter almonds and extracting to obtain oil and meal; soaking almond meal in ethanol, extracting and filtering to obtain amygdalin extract and first residue and crystallizing to obtain crystal and first filtrate; adding ethanol to first residue, extracting, filtering to obtain total flavonoids extract and second residue, concentrating, dispersing in crude drug, passing in resin column, dispersing crude drug, passing in polyamide column and drying to obtain flavonoids; and drying second residue to obtain proteins.    USE - Simultaneous extraction of multiple active ingredients.    ADVANTAGE - The method is environment-friendly and increases utilization ratio of bitter almond.    DETAILED DESCRIPTION - Simultaneous extraction of multiple active ingredients comprises selecting bitter almonds, crushing and extracting to obtain bitter almond oil and bitter almond meal; soaking almond meal in 80-95% ethanol for 2-3 hours, incubating for 1-2 hours, extracting for 1-5 times, filtering while hot to obtain amygdalin extract and first residue, combining extracts were, concentrating under reduced pressure and crystallizing to obtain crystal and first filtrate, where crystal is laetrile; adding 50-80% ethanol to first residue, incubating in micro-boiling state for 1-2 hours, extracting 1-5 times, filtering while hot to obtain total flavonoids extract and second residue, combining total flavonoids extract to first filtrate, concentrating to recover solvent, adding water, dispersing in 0.4-1 g of crude drug/ml, passing in macroporous resin column, adding water, dispersing in 0.1-0.4 g crude drug/ml, passing in polyamide column, recovering solvent under reduced pressure and vacuum drying to obtain almond flavonoids; and drying second residue to obtain bitter almond proteins.
NOVELTY - Preparation of printing ink solvent and co-production of biodiesel comprises dehydrating waste animal and vegetable oil and removing impurities, conducting esterification reaction with alcohol under the action of acidic catalyst, reducing the acid value of waste animal oil and vegetable oil, transesterification reaction with lower alkyl alcohol under the action of alkaline catalyst, decompressing and rectifying, and separating fractions at less than 230 degrees C as diesel oil, fractions at 230-280 degrees C as ink solvent, and remaining bottom components as heavy fuel oil.    USE - Preparation of printing ink solvent and co-production of biodiesel (claimed).    ADVANTAGE - The production cost of plant oil-based printing ink is lowered. The prepared prinking ink solvent has good permeability and improves the defect of plant oil-based printing ink, which has low setting speed. High quality biodiesel is achieved.    DETAILED DESCRIPTION - Preparation of printing ink solvent and co-production of biodiesel by using waste animal oil and vegetable oil comprises dehydrating waste animal and vegetable oil and removing impurities, conducting esterification reaction with alcohol under the action of acidic catalyst, reducing the acid value of waste animal oil and vegetable oil to 3 mg potassium hydroxide (KOH)/g, transesterification reaction with lower alkyl alcohol under the action of alkaline catalyst to prepare crude fatty acid ester, decompressing and rectifying, and separating fractions at less than 230 degrees C as diesel oil, fractions at 230-280 degrees C as ink solvent, and remaining bottom components as heavy fuel oil.
NOVELTY - A water-soluble probenecid is processed by taking probenecid, adding alkaline matter to react, controlling temperature and pH value, filtering and drying.    USE - Method of processing water-soluble probenecid (claimed).    ADVANTAGE - The method has reduced production cost with improved quality and yield of product.
NOVELTY - A low b. pt. halogenated hydrocarbon gas is prepared by mixing an ionic liquid with urea, acetamide, priopionamide and/or caprolactam. The ionic liquid is aluminum chloride, zinc chloride or lithium chloride.    USE - Method of preparing a low b. pt. halogenated hydrocarbon gas, preferably methylene dichloride, trichloromethane, tetrachloromethane, dichloroethane, trichloroethane, 1,2-dichloroethylene, 1,1-dichloroethylene, trichloroethylene, vinyl chloride, dibromomethane, bromoethane, iodoethane or fluorobenzene (claimed) for an ionic liquid.    ADVANTAGE - The method is environment-friendly, can be applied to industrial production, has low energy consumption, and prepares hydrocarbon gas having b. pt. of 20-100 degrees C and absorbing pressure of - 600.325 to 101.325kPa and that is easy to recycle.
NOVELTY - Catalyst comprises 20-85 wt.% mesoporous silica-alumina zeolite and 15-80 wt.% bonding agent, where alpha value of catalyst is 25-50.    USE - The catalyst is useful for producing propane and high-octane gasoline through butane (claimed).    ADVANTAGE - The catalyst can convert butane into propane and by-product of high-octane gasoline blending components under specific reaction conditions, where the produced propane is utilized as ethylene cracking raw material and other chemical usages, and the produced high-octane gasoline blending components is utilized to adjust fluid catalytic cracking gasoline to reduce olefin content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the catalyst, comprising extruding and molding the mesoporous silica-alumina zeolite and bonding agent precursors after mixing, then drying and calcining, and treating with steam at 430-570 degrees C, where the mass ratio of the steam to calcined catalyst is 0.5-5.
NOVELTY - Wastewater sludge is dehydrated and dried to produce dried sludge with water content of 10 wt.% or less. The dried sludge is pulverized and mixed with water to increase the water content to 13-17 wt.% in the dried sludge surface. The dried sludge is compressed in a pellet molding device consisting of extrusion die to form pelletized sludge with water content of 11-15 wt.% and impact strength of 90 kg/cm2. The pelletized sludge is cooled and dried by counter flow method using air to obtain solid fuel with water content of 10 wt.% or less.    USE - Manufacture of solid fuel using wastewater sludge (claimed).
NOVELTY - Preparing bio-mass bi-component polyurethane, comprises adding 30-35 parts by mass (pbm) of refined glycerol, 40-60 pbm of rosin, 100 pbm of dihydric alcohol and 0.1-1 pbm of catalyst into a flask, heating, adding 15-30 pbm of succinic anhydride, heating and cooling the mixture to obtain polyester polyol, adding 100 pbm of polyester polyol and 30-50 pbm of polyester polyol-2000 into the flask to obtain component A, adding 80-100 pbm of polyester polyol and 10-30 pbm of toluene diisocynate in the flask, heating and cooling to obtain component B, and mixing the components A and B.    USE - The bio-mass bi-component polyurethane is useful as glue in a polyurethane foam laminboard (claimed) and for producing a biodiesel.    DETAILED DESCRIPTION - Preparing bio-mass bi-component polyurethane, comprises adding 30-35 parts by mass (pbm) of refined glycerol, 40-60 pbm of rosin, 100 pbm of dihydric alcohol and 0.1-1 pbm of catalyst into a flask, heating the mixture using a microwave with power of 600 W for 10-15 minutes, adding 15-30 pbm of succinic anhydride in the mixture, heating the mixture using a microwave with power of 800 W for 30-40 minutes until no water is distilled, cooling the mixture to obtain polyester polyol, adding 100 pbm of polyester polyol, 30-50 pbm of polyester polyol-2000, 0.1-0.5 pbm of dibutyltin dilaurate and 0.1-0.5 pbm of n,n-dimethylcyclohexylamine into the flask, stirring the mixture at room temperature for 30 minutes to obtain component A, discharging and packing the obtained component A, adding 80-100 pbm of polyester polyol and 10-30 pbm of toluene diisocynate in the flask, heating the mixture at 75-80 degrees C for 3 hours, cooling the heated mixture at room temperature to obtain component B, and hermetically packing and mixing the component A and the component B in a mass ratio of 1:1.
NOVELTY - Manufacture of resin pellets involves providing timber sawdust, filtering impurities from timber sawdust, adding resin (3-10%) to filtered timber sawdust and mixing, supplying mixture to extruder, pelletized and drying.    USE - Manufacture of resin pellets (claimed).    ADVANTAGE - The method efficiently and economically provides resin pellets.
NOVELTY - The method involves moving a piston in an axial direction of a cylinder. The cylinder is arranged at a cross section of 80 to 20 decimeters. First chamber and second chamber are separated by a piston that is arranged inside wall of the cylinder. Feeding wet biomass is maintained at low pressure that is less than 5 MP in the first chamber. The feeding wet biomass is transferred from the first chamber to the second chamber when the piston is moved on the cylinder.    USE - Method for feeding wet biomass.    ADVANTAGE - The method enables disposing vast quantities of animal manures, avoiding leakage of wet biomass present in the cylinder, and providing low-pressure pump for easy processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for feeding wet biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for packaging of cheese.
NOVELTY - Extracting lactic acid fermentation product of kitchen waste, involves preparing polyethylene glycol and dextran water solutions, mixing the two polymer water solutions, adding kitchen waste and lactic acid bacteria, and carrying out lactic acid fermentation, after the reaction finishes, standing the fermentation liquid, and calculating the extraction rate of lactic acid, and extracting the upper phase liquid, and recycling polyethylene glycol with an ultrafiltration membrane.    USE - The method is useful for extracting lactic acid fermentation product of kitchen waste, where the kitchen waste is liquid, semisolid or solid (claimed).    ADVANTAGE - The method is simple and rapid, and solves problem of high chemical raw material consumption and low final product yield.    DETAILED DESCRIPTION - Method for extracting lactic acid fermentation product of kitchen waste, involves respectively preparing polyethylene glycol and dextran water solutions with certain concentrations, mixing the two polymer water solutions to form a double-water-phase system, adding kitchen waste and lactic acid bacteria, and carrying out lactic acid fermentation under certain temperature conditions while continuously and evenly stirring, after the reaction finishes, standing the fermentation liquid, and calculating the extraction rate of lactic acid according to the volumes of upper phase and lower phase, and extracting the upper phase liquid, and recycling polyethylene glycol with an ultrafiltration membrane.
NOVELTY - The method involves performing agitation of coagulant in the organic material using a coagulant agitation vat (70). The agitated coagulant is mixed with a neutralizing agent. The cohesion sludge is transferred to specific side of vertical type air pressure dehydrator (90). The liquid phase object in sludge is dehydrated at the effluent transferred to dehydrator. The biogas is ejected to the sludge in digestion tank (150), so that the moisture is removed through an anaerobic microorganism of tank. The aggregate of liquid phase object is supplied through a nozzle.    USE - Method for removing organic material, nitrogen and phosphorus in high-concentration organic waste water of food waste or livestock excretion.    ADVANTAGE - The organic material, nitrogen and phosphorus in organic waste water can be removed easily. The accuracy and effectiveness of sludge dewatering process can be improved. The removal process of organic material, nitrogen and phosphorus in organic waste water can be simplified. The establishment area of removing apparatus can be minimized and the processing efficiency can be maximized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for removing organic material, nitrogen and phosphorus in high-concentration organic waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for removing organic material, nitrogen and phosphorus in high-concentration organic waste water. (Drawing includes non-English language text)    Mixer (11)    Transfer pipe (20)    Coagulating agitation vat (70)    Vertical type air pressure dehydrator (90)    Digestion tank (150)
NOVELTY - The utility model claims a condensing device, especially refers to a kind of marsh gas condensing device, comprising a shell body, wherein the shell is filled with glass beads, middle part or lower part of side of the shell is provided with marsh gas inlet, and the top of the shell is provided with a biogas outlet, one side of the bottom of the shell is further provided with a condenser, the outlet of the condensing end is provided with a valve, the utility model is compared with the existing technology, the cost of the equipment, that is, once is greatly reduced, it only needs to the PVC plastic film and a glass bead and so on simple material, it can be made into marsh gas condensing device, it is convenient and practical.
NOVELTY - This utility model relates to energy processing switch device. This utility model is the biomass gasification furnace is composed of storage bin 8, dilute 9, phase 6, an 1, a 3, 12 and a gas outlet 13 a, 8 is connected to the lower part of the feeding screw 7 and the phase 6, the phase 6 is , the bottom is provided with a air inlet pipe 1 and discharge pipe 3, dilute the 9 phase 6, the gas outlet 13 is located in the phase section 9 the lower part of the valve is provided with 14 dilute 9; with refractory material 10 the phase section 9 and phase 6 of the outer wall. This utility model cancels the in step a, separating the carbon powder does not return furnace, continuously gasifying and discharging the carbon powder adding adhesive pressing and forming carbon. A smart structure can effectively reduce the height of the gasification furnace, and it can reduce the manufacturing cost of the gasification furnace.
NOVELTY - This utility model claims a biomass gasification furnace positive and negative double-direction air inlet device, comprising a door (6), the air channel (13) and the lower air passage (5), the air channel (13) is the gas outlet (10) of the outlet passage surrounding annularly distributed, the lower air duct (5) is a feeding port (4) is distributed around the air passage (13) is connected with the upper (12) and lower air channel (5) is connected with the governing (3), upper (12) and lower air duct (5) is located in the hearth (2), the upper and lower positions of the several upper roof (12) is fuel gas outlet (10) is vertical annular distribution ring is cylinder-shaped, a lower air pipe (3) is a feeding port (4) is inclined annular distribution ring is upper (12) and governing air outlet (3) are respectively in the nozzle. This utility model is divided into upper and lower two layers of distribution to realize wind and wind pressure through upper and governing uniform, uniform, so it is good for controlling the temperature of the hearth is between 600 degrees and 650 degrees.
NOVELTY - 35 %Mass coal slurry, 5 %mass anthracite, 5 %mass raw coal, 50 %mass biomass raw material containing straw, saw dust, 4 %mass smoke desulfurization agent and 1 %mass quick-setting agent are uniformly mixed to obtain environmentally-friendly particulate coal briquette.    USE - Production of environmentally-friendly particulate coal briquette used for different types of furnaces.    ADVANTAGE - The production method is simple, safe and environmentally-friendly. The particulate coal briquettes are manufactured with reduced energy consumption, have excellent combustion property, excellent air permeability, fast flaming property, controllable heat value, low ash slag generation characteristics, easy cleaning property and low dust concentration.
NOVELTY - The device has a furnace body (18) provided with a material cavity (II). An anode unit (21) is arranged on the upper part of the furnace body. A top cover (2) is provided with a synthesis gas output interface (I). A cooling water inlet connector (25) is connected to a cooling water outlet connector (5) that is connected to the material cavity of the furnace body, where the material cavity is provided with raw material inlet that is formed with a spiral feeder discharge hole. A spiral rotating shaft (11) is provided with a spiral extruding plates in a feeding cylinder (10).    USE - Domestic rubbish and biomass gasification furnace device.    ADVANTAGE - The device converts domestic rubbish or biomass into hydrogen-rich high quality synthesis gas. The device removes dioxin pollution problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a domestic rubbish and biomass gasification device.    Synthesis gas output interface (I)    Material cavity (II)    Raw material inlet (1)    Top cover (2)    Cooling water outlet connector (5)    Feeding cylinder (10)    Spiral rotating shaft (11)    Furnace body (18)    Cathode unit (19)    Anode unit (21)    Cooling water inlet connector (25)
NOVELTY - This utility model claims waste purifying and energy recycle field. A kind of kitchen waste grease pre-treating system solves the problem that the oil separation efficiency is low, it can not carry out grease separating treatment for food residue, comprising a spiral extruding part slag, the raw material metering sampling tank, crude oil heating tank, hot mixing a pool, a centrifuge, a water mixing tank, a groove, a conveying pump, a storage tank and a conveying pump, a spiral extruding part slag according to the order is connected with the raw material metering sampling tank, crude oil heating tank, hot mixing a pool, a centrifuge, a water mixing tank, a centrifuge, a product middle groove, conveying pump, a finished product oil storage tank and conveying pump. The said a kind of kitchen waste grease pre-treating system is featured with simple structure, convenient operation, completely separating and purifying, and processing efficiency is high.
NOVELTY - This utility model is the organic material comprehensive processing system, comprising a material sieving device, a material crushing device, a material forming device, organic material dry distillation gasification furnace, carbonization primary washing tower, a secondary washing tower, a dry distillation self-cleaning heat exchanger. The beneficial effect of the utility model is, convenient to use, low cost, does not generate dioxin and heavy metal pollution, no waste slag, waste solid produced as smokeless fuel.
NOVELTY - This utility model claims a kind of removing tar type biomass fixed bed gasification furnace, comprising a vertically arranged with the furnace body, the furnace body from bottom to top in turn is conical hopper-shaped tail ash section, reaction section, a gas outlet is provided with tar removing section, removing the top of the detarring section, the reaction section is provided with a clapboard and a tar removing section, the upper part is provided with a baffle plate connected with the reaction section of the gas inlet is provided with a tar removing device for removing tar in a period of time, a condensing cylinder tar removing device, condensing tube comprises two end opening of the cylindrical shell, the lower end of the cylindrical shell body is connected with the baffle plate of the gas inlet, and a furnace wall, a baffle plate of coke oil section, a gas can not enter into the shell space of the coke oil device; in the cylindrical shell body is provided with a plurality of cooling tube to form the tube bundle, the removing tar type biomass fixed bed gasification furnace further comprises a water vapour pipeline can be connected to a cooling medium inlet, and for generating steam for the steam generator.
NOVELTY - This utility model claims a kind of is provided with a plurality of the focus area for removing tar type biomass fixed bed gasification furnace, comprising a vertically arranged with the furnace body, the furnace body from bottom to top in turn is conical hopper-shaped tail ash section, reaction section, a grate is provided with tar removing section, tail ash section and reaction section, and the top of the tar section is provided with a gas outlet, the tail section of the ash outlet is set at the bottom, the side part of the tail ash section is provided with at least one gasification medium inlet, and the reaction section of the upper side is provided with a feeding port, the tar in the there are two or more than two and the number of the coke oil device. A plurality of tar removing device in the furnace is capable of alternately using, when a tar removing device is tar blocking, it can close the tar removing device, and starting the other one tar removing device is closed the device will remove the tar oil in a gas with high temperature and/or steam heating, the wall of the tar will melt at high temperature, the material and the weight of the downstream function so as to finish the cleaning work of the fault condensing cylinder.
NOVELTY - This utility model claims a kind of removing tar type biomass fixed bed gasification furnace system, comprising a tar removing type biomass fixed bed gasification furnace from a vertically set with tar type biomass fixed bed gasification furnace of the furnace body, the furnace body from bottom to top in turn is conical hopper-shaped tail ash section, reaction section, a tar removing section, tail ash section and reaction section is provided with a fire grate, the top of the tar section is provided with a gas outlet, the bottom of the section is provided with a tail ash outlet, the side part of the tail ash section is provided with at least one gasification medium inlet, and the reaction section of the upper side is provided with a feeding port, and the reaction section and the upper part is provided with a clapboard and a detarring section, provided with a reaction gas inlet section is provided with a tar removing device for removing tar in a period of time, a condensing cylinder tar removing device, condensing tube comprises two end opening of the cylindrical shell, the lower end of the cylindrical shell body is connected with the baffle plate of the gas inlet, and a furnace wall, a baffle plate of coke oil section, a gas can not enter into the shell space of the coke oil device; in the cylindrical shell body is provided with a plurality of cooling tube to form a tube beam, a plurality of cooling pipe is vertically hung at intervals, the upper end opening of the cylindrical shell body is connected with fuel gas pipeline, a gas pipeline is connected to the gas outlet.
NOVELTY - This utility model claims a biomass fixed bed gasification furnace tar removing device, wherein the device comprises a tar condensing tube, the condensing tube comprises two end opening of the cylindrical shell, the lower end of the cylindrical shell is a gas inlet, in the cylindrical shell body is provided with a plurality of cooling tube to form a tube bundle, a plurality of cooling pipe is vertically hung at intervals, the upper end opening of the cylindrical shell body is connected with fuel gas pipeline, a gas pipeline is connected to the gas outlet. Compared with the existing technology, the utility model has the following beneficial effects: 1, it does not affect the production efficiency of the gas, but also will not cause pollution to the outside environment and the environment water cycle, 2, gas temperature of the first drying layer part is used for fuel in the furnace to dry, so the cooling circulating water to take away the heat, wherein a gas cooling process, large amount of tar recycle and gasification in, which dramatically improves the energy utilization rate, compared to save a cooling loss, 3, the gas temperature is low, a pair of auxiliary meter and pipeline and so on is reduced greatly, saves the investment cost.
NOVELTY - This utility model claims a kind of is provided with return gas heating section biomass fixed bed gasification furnace, the biomass fixed bed gasification furnace comprises a return gas heating section furnace body and the longitudinal direction, the furnace body comprises a conical hopper-shaped tail ash section, reaction section, the upper part of the reaction section is provided with a feeding port, the tail ash section and reaction section is provided with a fire grate, the side part of the bottom of the section is provided with a tail ash outlet, the tail ash is equipped with at least one gasification medium inlet, the top of the furnace body is provided with a fuel gas outlet, reflux gas heating section is a jacket surrounding the reaction section of the furnace body, wherein a gas inlet and a gas outlet, reflux gas heating gas inlet is directly or indirectly connected to the top of the furnace body through a pipeline of the gas outlet. This utility model, through a reflux gas heating section, the temperature of the furnace gas to heat, so as to reduce the heat loss and improve the efficiency of the gasification furnace.
(CN203128509-U)   NOVELTY - This utility model claims a kind of a gasification medium is biomass fixed bed gasification furnace, comprising a steam generator and a furnace body is vertically provided with, the furnace body comprises a conical hopper-shaped tail ash. (including air), reaction section, a steam generator is a jacket surrounding the reaction section of the furnace body, and comprises at least one inlet and at least one outlet, and the reaction section of the upper side is provided with a feeding port, the tail ash section and reaction section is provided with a fire grate, the bottom part of the section is provided with a tail ash outlet, the tail ash is provided with gasification medium inlet, gasification medium inlet is connected to at least one outlet of the steam generator through the pipeline. A generator furnace temperature, the water is heated to steam, the steam can take part in the reaction from the furnace bottom of the gasification medium inlet into the furnace, so as to improve the heat value of the fuel gas generation.
NOVELTY - This utility model claims a steam generator for removing tar type biomass fixed bed gasification furnace, comprising a vertically arranged with the furnace body, the furnace body from bottom to top in turn is conical hopper-shaped tail ash section, reaction section, a tar removing section, removing tar type biomass fixed bed gasification furnace further comprises a steam generator, a steam generator is a jacket surrounding the reaction section of the furnace body, and comprises at least one inlet and at least one outlet. The steam generator furnace temperature, the water is heated to steam, the steam can take part in the reaction from the furnace bottom of the gasification medium inlet into the furnace, so as to improve the heat value of the fuel gas generation, or can use the steam cooling pipe, that is, the steam passes through the cooling pipe, so as to make the condensed tar cooling pipe is heated and becomes fluid flow, and returning the reaction from the gas inlet on the clapboard continuously take part in the reaction, at the same time, the self-cleaning of the condensing tube.
NOVELTY - The utility model claims a combined type biomass fuel rod, comprising a core rod, wherein the core rod is coated with combustion-supporting layer is provided with a combustion space in the core rod, and the core rod and the combustion-supporting layer is provided with a combustion-supporting structure. Thus, because of a stick-shaped core material, for delivery, storage and transmission, are capable of automatic control. At the same time, the whole body is solid particles, large power density, small volume, high flash point, is safe and convenient, and clean. And fuel volatile combustion property, high burn-off.
NOVELTY - The utility model claims a combined type biomass fuel block, comprising a central carbon block, wherein the central carbon block is covered with a layer, composed of fuel block main body is provided with a combustion space of the central carbon block, and between the carbon block and the combustion-supporting layer is provided with a combustion-supporting structure. Thus, because a flat core material, for delivery, storage and transmission, are capable of automatic control. At the same time, the whole body is solid particles, large power density, small volume, high flash point, is safe and convenient, and clean. And fuel volatile combustion property, high burn-off.
NOVELTY - The device (1) has a top and bottom opened annular apron (30) i.e. ring gas accumulator, to which solid material is supplied over a pneumatic lock. The apron comprises an inner jacket (31) and an outer jacket (32), where a cooling gap (33) is formed between the jackets for supply and removal of cooling medium i.e. water. The inner jacket and the outer jacket are connected with each other at a bottom side facing a bed (12) fixed in a reactor. The cooling gap is covered by a cover (40) at an upper edge of the apron, which is turned away from the fixed bed.    USE - Device for filling a reactor with pressurized carbonaceous solid material e.g. charcoal, biomass and petroleum, for gasification of the carbonaceous solid material.    ADVANTAGE - The cooling gap is formed between the inner jacket and the outer jacket of the apron for supply and removal of the cooling medium, so that the service life of the apron is increased even when the apron is used at gasification temperature above 450 degree Celsius and/or with fuel containing sulfur and/or halogen. The provision of the cooling gap allows compensating frequent temperature peaks without forcing a load depression or a shorter and/or prolonged shutdown of the reactor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a reactor for gasification of a carbonaceous solid material    (2) a method for gasification of a carbonaceous solid material.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a ring gas accumulator.    Filling device (1)    Bed (12)    Top and bottom opened annular apron (30)    Inner jacket (31)    Outer jacket (32)    Cooling gap (33)    Cover (40)
NOVELTY - The method involves introducing water vapor into a fluidized-bed furnace (S300) from a water vapor introduction part, and fluidizing a flow medium with water vapor. Calcium substance i.e. biomass ash, comprising precursor of calcium oxide is introduced in the flow medium fluidized with the water vapor, and a catalytic function is added to the flow medium (S310). A gasifying agent and gasification raw material are introduced into a fluidized-bed furnace, and gasifying gas is generated (S340) after adding the catalytic function to the flow medium.    USE - Method for generating gasifying gas utilized for various applications by gasifying gasification raw material. Uses include but are not limited to electric power generation system, manufacture of hydrogen, manufacture of synthetic fuel i.e. synthetic petroleum and manufacture of chemical e.g. chemical fertilizer such as urea, by gasifying coal i.e. wood coal, petroleum coke, biomass and tire chip.    ADVANTAGE - The method enables reducing generation of tar and residue in a gasifying gas generation system by adding the catalytic function to the flow medium before generating the gasifying gas using the gasification raw material, thus improving gasification efficiency of the gasification raw material.    DETAILED DESCRIPTION - The gasifying agent is selected from water vapor, nitrogen, air, oxygen and carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a gasifying gas generation method.'(Drawing includes non-English language text)'    Step for introducing water vapor into fluidized-bed furnace (S300)    Step for adding catalytic function to flow medium (S310)    Step for performing gasifying agent fluidized-bed formation process (S320)    Step for generating gasifying gas (S340)
NOVELTY - This utility model claims a kind of the marsh gas recycling device, comprising a pool and a gas pipe, further comprising a first filter pool and the second filter tank, the first gas pipe extends to the bottom of the first filter tank is divided into a plurality of first air outlet pipe, the upper end of the first filter is connected with the second tank is provided with a gas pipe, the second gas pipe extends to the bottom of the second filter tank is divided into a plurality of second air outlet pipe, a filter upper end is provided with an air outlet, the first filter pool and the second filter pool are provided with filter liquid. According to the technical solution of the utility model, the purity can be obtained by carrying out a filtering of the marsh gas to recycle higher marsh gas, and the air outlet of the air outlet pipe is an air outlet is composed of multiple round holes, the recovery of other disperse to filter to the filter tank, the filtering effect is better.
NOVELTY - Manufacture of straw fuel column involves removing dust impurity from soybean straw through vibrating screen, crushing dust impurity-removed soybean straw using crusher into crushed aggregates having desired length, mixing crushed material, naturally drying in dryer, until moisture content becomes 15-16%, granulating dried and crushed soybean straw into granulator to produce straw fuel column, placing straw fuel column into cooling tank, cooling to normal temperature using forced air, processing using vibration sieve, placing obtained material in pelletizer, and packing.    USE - Manufacture of straw fuel column (claimed).    ADVANTAGE - The method provides straw fuel column with reduced carbon emission. The straw fuel column can be used as substitute for coal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for straw fuel column, which has diameter of 1-1.3-1.5 cm, and length of 0.5-5 cm.
NOVELTY - The sample pool has a cooling shell provided with a shell body. The shell body is provided with a transverse air outlet pipe. An end of a cylinder body is fixed on an inner wall of a sleeve ring. The sleeve ring is provided with a fixing ring. A wall end of the cylinder body is detachably provided with a circular fixed lantern ring. Round heat preservation plugs are made of polyethylene material or quartz material and respectively fixed on two ends of the cylinder body, where shape and size of the plugs are identical. A sealed cavity is filled with a cooling medium.    USE - Terahertz spectroscopic natural gas hydrate detecting sample pool.    ADVANTAGE - The sample pool ensures normal pressure condition at normal temperature, and detects natural gas hydrate in a simple and economic manner.    DETAILED DESCRIPTION - The cooling medium is one of liquid nitrogen or ethylene glycol. The fixing and fixed rings are made of same metal or alloy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a natural gas hydrate detecting sample pool.
NOVELTY - The generator has a ramp-up section electrically connected with a fuel cell portion through a first switch. A control unit controls a second switch for turning-on the second switch to charge a battery. A thermal resistor is connected to the battery through the second switch. The battery stores surplus power generated in the ramp-up section by moving the fuel cell portion. The fuel cell portion produces electricity based on electro chemical reaction of fuel and the oxidizing agent through the thermal resistor.    USE - Molten carbonate-type fuel cell power generator.    ADVANTAGE - The generator can generate surplus power.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a molten carbonate-type fuel cell power generator. '(Drawing includes non-English language text)'
NOVELTY - Producing improved fuel product, comprises: obtaining bio-oil generated from processing biomass; performing first phase of pretreatment on the bio-oil, where the first phase includes at least oxidation step configured to increase carboxylic acid content in bio-oil or acid anhydride step configured to convert water to carboxylic acids, thus increasing product acidity and reducing water content in the bio-oil; and implementing second phase of treatment on intermediate product, where second phase of treatment includes at least one step e.g. partial deoxygenation step.    USE - The method is useful for producing an improved fuel product (claimed) comprising boiler fuel and transportation fuels.    ADVANTAGE - The method: is cost effective, increases fuel yield, and provides more fungible fuels; and reduces coking, thus prolonging catalyst life.    DETAILED DESCRIPTION - Producing an improved fuel product, comprises: obtaining a bio-oil generated from processing biomass; performing a first phase of pretreatment on the bio-oil, where the first phase includes at least an oxidation step configured to increase carboxylic acid content in the bio-oil or an acid anhydride step configured to convert water to carboxylic acids, thus increasing product acidity and reducing water content in the bio-oil, where an output of the first phase of pretreatment is an oxidized product or a hyper-acidified product; and implementing a second phase of treatment on the intermediate product, where the second phase of treatment includes at least one step comprising a partial deoxygenation step, a full deoxygenation step, a decarboxylation step, an esterification step, an olefination/esterification step, and a hydroprocessing step which are configured to improve fuel yield and energy density in a final fuel product. An INDEPENDENT CLAIM is also included for a composition obtained by the method.
NOVELTY - The hybrid cell apparatus has a first battery module (110) which is provided for transmitting heat in the process of generating electricity. A second battery module (150) is provided for receiving heat through thermal medium to generate the fuel. A heat exchanger (130) is provided for delivering heat emitted in the first battery module to the thermal medium. A tank is provided for storing the fuel generated in the second battery module and supplying the stored fuel to the first battery module.    USE - Hybrid cell apparatus.    ADVANTAGE - The fuel can be generated efficiently using the hybrid cell apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hybrid cell apparatus. (Drawing includes non-English language text)    First battery module (110)    Heat exchanger (130)    Pump (133)    Second battery module (150)    Power source (340)
NOVELTY - The system has a fuel supply part feed hydrocarbon fuel from a fuel cell stack for producing reforming fuel into hydrogen. A control unit is connected with a power source that is connected with multiple motor valves. A switch is connected with multiple motor valves. The control unit controls the switch based on switching state of temperature information of the fuel cell stack. A temperature sensor detects the temperature of a reformer. The reformer reforms the fuel into hydrogen by using chemical reaction of hydrogen and air.    USE - Fuel cell system.    ADVANTAGE - The system prevents the inner section from being damaged, and has better durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for driving a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system.'(Drawing includes non-English language text)'
NOVELTY - Aerosol device comprises a cosmetic composition including water-insoluble calcium salts, fixing polymers, 2-4C monoalcohols, and propellants.    USE - The aerosol device is useful for spraying cosmetic composition on wet or dry hair for shaping hair and/or maintaining hairstyle (claimed).    ADVANTAGE - The aerosol device does not freeze the hair, restores the shape of the hair, and remodels the hairstyle during the day without additional application of the composition.
NOVELTY - Production of phosphoric acid using low grade phosphorite and wet-process, involves mixing low grade phosphate ore slurry with phosphoric acid, separating, extracting clear liquid and filter residue through solid-liquid separation; extracting clear liquid with sulfuric acid, separating solid from liquid to obtain phosphoric acid and phosphogypsum; returning phosphoric acid for decomposing phosphorite and phosphoric acid as product output; washing ore slurry and phosphogypsum with water to form washed filter residue to obtain high quality white phosphorus gypsum; and washing with water.    USE - For production of phosphoric acid (claimed) widely applied to industrial phosphate and pigmentation fertilizer industry.    ADVANTAGE - Using low grade phosphorite, the method produces a high quality phosphoric acid in high yield, and has industrial application prospect.    DETAILED DESCRIPTION - Production of phosphoric acid using low grade phosphorite and wet-process, which is a two-step reaction including counter-current washing process and wet process, involves mixing low grade phosphate ore slurry with phosphoric acid, separating, extracting clear liquid and filter residue through solid-liquid separation; extracting the clear liquid with sulfuric acid, separating solid from liquid to obtain phosphoric acid and phosphogypsum; returning phosphoric acid for decomposing phosphorite and phosphoric acid as a product output; washing ore slurry and phosphogypsum with water to form washed filter residue to obtain the high quality white phosphorus gypsum, and washing with water to form phosphoric acid.
NOVELTY - A biomass pyrolysis oil modification method involves breaking layering, removing water, and adding an inorganic salt ion and an organic demulsifier to biomass pyrolysis oil. The mixture is stirred. The upper biomass pyrolysis oil and lower layer aqueous solution are separated for taking out the biomass pyrolysis oil. Catalytic cracking is performed on the pyrolysis oil. Ageing treatment is performed on zeolite molecular sieve loaded clay modified catalyst. The aged catalyst is placed in the reactor, and the biomass pyrolysis oil is injected into the reactor.    USE - Method for modifying biomass pyrolysis oil.    ADVANTAGE - The method enables modifying the biomass pyrolysis oil in an effective manner.    DETAILED DESCRIPTION - A biomass pyrolysis oil modification method involves breaking layering, removing water, and adding an inorganic salt ion and an organic demulsifier to biomass pyrolysis oil. The mixture is stirred. The upper biomass pyrolysis oil and lower layer aqueous solution are separated for taking out the biomass pyrolysis oil. Catalytic cracking is performed on the pyrolysis oil. Ageing treatment is performed on zeolite molecular sieve loaded clay modified catalyst for 2-8 hours at 500-800 degrees C. The aged catalyst is placed in the reactor, and the biomass pyrolysis oil is injected into the reactor, where mass ratio of the inorganic salt to the biomass pyrolysis oil is 1: 2000-1:800 and mass ratio of organic emulsion splitter to biomass pyrolysis oil is 1: 4000 -1: 1000, agent-oil ratio is 1: 3-16, reaction temperature is 380-700 degrees C and the reaction pressure is 0.1-0.8 MPa.
NOVELTY - Organisms combustion improver comprises 35-45 wt.% black shale, 35-45 wt.% potassium chlorate, 3-10 wt.% industrial salt, 8-12 wt.% charcoal and 3-5 wt.% manganese dioxide.    USE - Organisms combustion improver.    ADVANTAGE - The organisms combustion improver has high energy, reduced biomass fuels consumption, high economic value and increased thermal efficiency. The improver is free from pollution, toxic generation and environment-friendly.
NOVELTY - Use of additive(s) with detergent action is claimed. The additive is compound with groups derived from succinic anhydride, and hydroxyl, amino, amido and/or imido groups, nitrogen compound quaternized in an acid-free manner, or polytetrahydrobenzoxazine and bistetrahydrobenzoxazine for increasing fuel oil. The nitrogen compound quaternized in an acid-free manner is obtained by quaternizing by adding compound having at least one oxygen- or nitrogen- containing group reactive with anhydride and quaternizable amino group(s) to polycarboxylic anhydride compound.    USE - Use of additive for increasing cetane number of cetane number improver-containing fuel oil e.g. diesel oil and mixture of biofuel oil and intermediate distillate of fossil, vegetable or animal origin for internal combustion engine e.g. diesel engine.    ADVANTAGE - The generation of deposit in an internal combustion engine is prevented, using additive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel additive concentrate, which consists of 5-45 wt.% additive, 20-90 wt.% cetane number improver(s), 5-35 wt.% organic diluent(s) or solvent(s) chosen from aromatic, aliphatic hydrocarbons and alcohols, 0-10 wt.% customary co-additive(s) chosen from corrosion inhibitors excluding mixtures of 12-24C aliphatic saturated or unsaturated monocarboxylic acid or dimerization or trimerization and their products, which is optionally present in the form of free carboxylic acid and/or in the form of ammonium salt, amide, ester and/or nitrile, and polycyclic hydrocarbon compound which are obtained from distillation residue of natural oil which is extracted from tree resin, demulsifier, dehazer, antifoam, antioxidant and stabilizer, metal deactivators, antistat, lubricity improver, and dye and marker. The sum of all components is 100 wt.%.
NOVELTY - Fixed bed biomass gasification furnace relates to biomass gasification furnace with raw fuel gas outlet device of the spiral feeding machine. A rotary valve (1), a spiral feeding machine (2), a biomass gasification furnace (4), a spiral feeding machine (2), the output end is inserted into biomass gasification furnace (4), which are welded with the shell of the spiral feeding machine (2) are respectively welded with a rough fuel gas outlet pipe (3) and a feeding pipe (5), the feeding pipe (5) is set with a rotary valve (1), a flange by a bolt. A gas outlet of the biomass gasification furnace is set on the spiral feeding machine, mixed gas in order to prevent the air in the storage hopper, the thermal value, the material feeding tube is provided with a rotary valve as a gas seal. It has simple and compact structure, effectively reduces the gas temperature and purifying gas and so on.
NOVELTY - Taking-off free cleaning agent of intraoral prosthesis, comprises 75 pts. wt. deionized water, 15 pts. wt. infiltration agent, 5 pts. wt. tea polyphenol, 2 pts. wt. surfactant, 1 pts. wt. polyvinyl methyl ether/maleic anhydride (PVM/MA) copolymer, 0.5 pts. wt. Stevia, 0.5 pts. wt. sodium benzoate, 0.05 pts. wt. sodium monofluorophosphate, 0.005 pts. wt. bacteriostatic agent, and pH regulator (specific amount).    USE - Used as taking-off free cleaning agent of intraoral prosthesis.    ADVANTAGE - The cleaning agent: directly cleans the oral prosthesis; has no damage to various oral prosthesis; prolongs the service life of the oral prosthesis; can effectively sticking and killing oral bacteria to prevent denture stomatitis; and is environmentally friendly, non-toxic, neutral in pH, harmless to mouth mucosa and safe to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the taking-off free cleaning agent of intraoral prosthesis, comprising (a) mixing deionized water, tea polyphenol, Stevia, sodium benzoate, sodium monofluorophosphate and bacteriostat agent, stirring until the solution is clear, and filtering to obtain aqueous-based raw material; (b) mixing infiltration agent, surfactant and PVM/MA copolymer, stirring for 24 hours until the solution is clear, and using supernatant as organic raw material; (c) stirring the aqueous-based raw material, and slowly adding to the organic raw material to avoid air bubbles, and mixing them uniformly to obtain master batch; and (d) adjusting the pH of the master batch with the pH regulator to 7 to obtain the finished product.
NOVELTY - A sawn wood is supplied into detachable container having openings, dried, subjected to pyrolysis and cooled, to obtain charcoal. The wood feedstock is loaded evenly with dense packing, and pyrolysis steam gases are forcedly supplied into container with subsequent reversed movement of heat-transfer agent.    USE - Preparation of charcoal (claimed).
NOVELTY - The system comprises a loading chamber, a processing chamber, and a linearly arranged unloading chamber. An ion gun stainless steel base metal is fixed to both sides of the processing chamber and to a movable carrier of the loading chamber, and coats the graphite phase carbon on the base material while moving the carrier. The processing chamber comprises a heater, and is arranged on a rectangular metal arc, and coats graphite-phase carbon on a metal nitride layer or a buffer layer. A vacuum chamber is placed between the loading chamber and the process chamber.    USE - The system is useful for manufacturing a fuel cell bipolar plate (claimed).    ADVANTAGE - The system is capable of efficiently manufacturing the fuel cell bipolar plate with excellent corrosion resistance and conductivity and high productivity.    DETAILED DESCRIPTION - The system comprises a loading chamber, a processing chamber, and a linearly arranged unloading chamber. An ion gun stainless steel base metal is fixed to both sides of the processing chamber and to a movable carrier of the loading chamber, and coats the graphite phase carbon on the base material while moving the carrier. The processing chamber comprises a heater, and is arranged on a rectangular metal arc, and coats graphite-phase carbon on a metal nitride layer or a buffer layer. A vacuum chamber is placed between the loading chamber and the processing chamber. A cooling chamber is installed between the processing chamber and the unloading chamber.
NOVELTY - Removing pesticides from contaminated water, comprises contacting the water with reduced graphene oxide (RGO) and/or graphene oxide (GO).    USE - The method is useful for removing pesticides from contaminated water such as ground water, industrial water or municipal water, where the pesticide includes organochlorine, organophosphate, organocarbomate, biopesticides and/or synthetic pyrethroid and the contaminant includes insecticides, fungicides, weedicides and rodenticide (all claimed).    ADVANTAGE - The method is capable of economically removing the pesticides from the contaminated water with high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) regenerating pesticide loaded RGO and/or GO comprising contacting the loaded RGO and/or GO with organic solvents, preferably ethanol; and    (2) a water treatment medium.
NOVELTY - A supported catalyst comprises a carrier, and an active metal component including group VIB metal component and group IB metal component.    USE - Supported catalyst is used for hydrofining biomass alcoholysis heavy oil (claimed).    ADVANTAGE - The supported catalyst has excellent catalytic activity when used in biomass alcoholysis heavy oil hydrofining. The stability and energy density of biomass alcoholysis light oil are greatly enhanced. The catalyst has long service life and can be easily regenerated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of supported catalyst, which involves contacting the metal components with a carrier, and drying and baking the carrier.
NOVELTY - The method involves preparing dried fiber into materials of required specification by using special bar machine. The bar materials are carbonized by using a high-temperature, high-efficiency and environment-friendly carbonizing furnace. Specific portion of residues are grinded and combusted through combustible gas recovery generation device. The combustible gas is recycled in carbon heating process. Residual carbides for producing gas are recycled after combustion of residues. Hot water is recycled from heat exchange after carbonization.    USE - Method for realizing intensive production and comprehensive utilization of forestry residues.    ADVANTAGE - The utilization ratio of wood processing can be improved to produce high-quality raw charcoal, machine-made charcoal, active carbon and other products with high additional value. The transport cost of forestry residues can be reduced. The industrialization application of combustible gas recovery generation device can be improved.
NOVELTY - A kind of disease livestock and poultry dead harmless processing workshop, the workshop comprises preparing pool, pedestrian passageway and arched roof, the bottom of the composting tank is provided with a filling layer, inner part is built around the baffle. The beneficial effects of the utility model lie in: harmless processing workshop stacking process according to a high temperature decomposing inoculant so as to design, uses a brick and concrete wall body and the arched roof structure is combined with the resin sunlight tile is provided with good lighting, so as to ensure the time for padding the fermentation temperature, can prevent rainwater flowing into the stack, the plant has simple structure, convenient construction, short construction period, reduces cost and saves investment.
NOVELTY - The system has reaction chamber (2), and wastewater inlet that is located at bottom portion of reaction chamber. An upright-cylinder-shaped polypropylene fiber carrier (4) is internally located in reaction chamber. A baffle plate (6) is arranged on outlet position of reaction chamber. An air outlet of reaction chamber is located at top end. A liquid outlet is placed at side wall.    USE - Industrial sewage comprehensive treatment system.    ADVANTAGE - The microorganism concentration in the reaction chamber is increased, average staying time of sludge is effectively prolonged and treatment efficiency of wastewater is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the industrial wastewater comprehensive treatment system.    Reaction chamber (2)    Upright-cylinder-shaped polypropylene fiber carrier (4)    Baffle plate (6)
NOVELTY - Preparing hemicellulose comprises crushing wood fiber raw material particle, mixing lignocellulose and wood fiber raw material particle with water, drying, sterilizing, culturing white rot fungus strain in agar culture medium, covering the surface with mycelium, mixing the wood fiber raw material with deionized water, stirring, filtering to collect water phase and residual solid component, decompressing and concentrating to obtain concentrated solution, adding ethanol to 2-4 times of the concentrated solution, reacting, centrifuging, and separating.    USE - The hemicellulose is useful for producing biofuel, and preventing timber resources from microbial degradation.    ADVANTAGE - The hemicellulose has galactose content of 21.7-42.1%, glucose content of 4.7-20.8%, uronic acid content of 13-15.4%, galacturonic acid content of 6-8.2%, polydispersity index of 1.4-1.8 and high yield, and is simply prepared.    DETAILED DESCRIPTION - Preparing hemicellulose comprises crushing wood fiber raw material particle into 20-40 meshes, mixing lignocellulose and wood fiber raw material particle with water for 10-30 minutes, drying, sterilizing at high temperature, culturing white rot fungus strain in agar culture medium comprising 2% pts. wt. of malt sugar at 28 degrees C for 4-16 weeks, covering the surface with mycelium, mixing the wood fiber raw material with deionized water for 4 hours, continuously stirring, filtering to collect water phase and residual solid component, decompressing and concentrating to obtain concentrated solution, adding ethanol to 2-4 times of the concentrated solution, reacting at 4 degrees C 8-16 hours, centrifuging, and separating.
NOVELTY - Hollow type sealing strip of engineering plastic biogas digester comprises a uniform hollow fin-shaped part and a circular part on both sides of its middle part.    USE - Used as a hollow type sealing strip of engineering plastic biogas digester.    ADVANTAGE - The sealing strip has good gas tightness, toughness and strength; and reduces the possibility that the sealing strip is misplaced between planes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hollow type sealing strip of engineering plastic biogas digester.
NOVELTY - Preparation of biodiesel lubricating oil comprises using catalyst, biodiesel and modified epoxy to prepare epoxy biodiesel; using epoxy biodiesel and long chain fatty acid in the presence of catalyst; and carrying out open-ring modified heterogeneous esterification reaction to obtain alcohol ester-based lubricant.    USE - Method for preparing biodiesel lubricating oil (claimed).    ADVANTAGE - The solid acid catalyst is stable, separates easily and is environment-friendly.
NOVELTY - The system has a chamber (3) having upper and lower portions. The lower portion receives a biomass and has grinding elements, cutting elements and an air input. The upper portion has partition with inner chamber generally centered within an outer chamber. The outer chamber has a first outlet and inner chamber has a second outlet. Flange (21) connects lower portion with inner and outer chambers. Airflow loop has a source of input air in lower portion. Light biomass particles propelled up from inner chamber to second outlet.    USE - System for conditioning raw biomass used as source of thermal energy to produce bio-plastics and other renewable bio-products, for residential, institutional and industrial buildings and biomass industry.    ADVANTAGE - As the airflow loop has source of input air in lower portion, and the light biomass particles propelled up from inner chamber to second outlet, the raw biomass can be conditioned efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass conditioning method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for conditioning raw biomass.    Chamber (3)    Sizer (8)    Inner cylinder (16)    Flange (21)    Feeding conveyer (300)
NOVELTY - The system has a condenser fluid bed reactor condensing bio stock from gas fed to a gas distribution plate. A biomass feeder supplies biomass, and is equipped to a side of the reactor. The reactor rapidly heat-decomposes the biomass by utilizing square column-shaped fluid yarn and cracks gas of the biomass. An outlet discharges the gas, and is equipped in the side of the reactor. A heater heats up inside and outside of the reactor. A square pillar shaped cyclone is arranged in the reactor. A vent is installed in an upper portion of an expanded solid-state layer of the reactor.    USE - Bio-crude oil manufacturing system.    ADVANTAGE - The system can improve rapid thermal degradability, so that the bio stock can be manufactured with high yield and high quality. The system enables manufacturing bio-crude oil in an easy manner, draws optimal driving condition to rapid thermal decomposition process phase, reduces system unit cost and improves processing efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bio-crude oil manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio-crude oil manufacturing system.
NOVELTY - A thermal accumulating type combined heat-carrying biomass charcoal gas-oil co-production pyrolysis system comprises biomass raw material preparation device, biomass pyrolysis device, product collecting device, and waste gas treatment device. The biomass pyrolysis device comprises dry ash furnace, moving bed pyrolyzing furnace, and heat-carrying medium heating device.    USE - Thermal accumulating type combined heat-carrying biomass charcoal gas-oil co-production pyrolysis system.    ADVANTAGE - The system can improve product quality, heat efficiency, and reduce gas processing power and processing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the system.
NOVELTY - A gas-solid joint biomass partition speed control pyrolysis system comprises biomass raw material preparation device, biomass pyrolysis device, biomass collecting device, and waste gas treatment device. The biomass pyrolysis device comprises dry ash removing furnace, heat pyrolyzing furnace, and heat decomposition furnace. The biomass pyrolysis device has three partition devices.    USE - Gas-solid joint biomass partition speed control pyrolysis system.    ADVANTAGE - The system can improve product quality and heat efficiency, and reduce gas processing power consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of using the system.
NOVELTY - Manufacture of biomass liquefied oil comprises primarily cooling mixed biomass pyrolysis gas and liquefying by oil injection in primary cooling system, and secondarily cooling and liquefying by oil injection in secondary cooling system; and controlling cooling temperature of primary cooling system at 100-200 degrees C to obtain high-grade liquefied oil, or controlling secondary cooling system at 0-60 degrees C to obtain low-grade liquefied oil.    USE - Method for manufacturing biomass liquefied oil (claimed).    ADVANTAGE - The method can fully utilize large quantity of straws and branches of wood. The liquefied oil has low cost and high quality.
NOVELTY - The method involves drying shredded municipal waste and/or an organic material. The dried municipal waste and/or the organic material are processed in a separation unit. An evaporator is connected with a turbine mixer. A catalytic depolymerization of the waste and/or the organic material is carried-out in the turbine mixer. The depolymerized material is distilled in a distiller (109) to obtain bio-components. A portion of the resulted bio-components is consumed to a power diesel-electric generator.    USE - Method for producing bio-components and biofuels in catalytic depolymerization.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for producing bio-components and biofuels in catalytic depolymerization. '(Drawing includes non-English language text)'    Distiller (109)
NOVELTY - The method involves forming compressed straw or energy crops in bales, and forming moisture up to 40 percentages in gasification process. A biomass is processed in an initial phase of the gasification process and a combustion process at temperatures from 450 degree Celsius to 800 degree Celsius. Required energy flux is obtained by an average working device.    USE - Method for producing stream of energy from uncrushed biomass.    ADVANTAGE - The method enables providing required quality of content of exhaust, and ensuring automatic working stages of a process correlate system.
NOVELTY - Simultaneous transformation of organic fraction of household solid waste into fertilizer and biogas includes front desk of rate structure design (1) in recycling industry with screening mat (2). Inorganic materials are separated by pouring it into an aeration tank (3), which is provided for dosing aqueous liquid utilized in the tank in batch digesters. The digesters are made of masonry, concrete, plastic or mixed materials, which perform natural process of anaerobic digestion.    USE - Method for simultaneous transformation of organic fraction of household solid waste into fertilizer and biogas used as a source of energy (all claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a rate structure design.    Front desk of rate structure design (1)    Screening mat (2)    Aeration tank (3)    Anaerobic chamber (4)
NOVELTY - This utility model claims a kind of multi-functional biomass gasification furnace. The multifunctional biomass gasification furnace comprises a storage box, a furnace body, a liner and a gas pipe, wherein a storage box is located at the upper part of the multifunctional biomass gasification furnace, wherein the inner container is located between the furnace body and the inner container is connected with the material storing tank, the inner container is 80 to 200 mm, wherein the gas pipe passes through the furnace body is connected with the inner container. This utility model is good for improving the gas quality, reduces the tar content in the fuel gas, and the gasification stability.
NOVELTY - A double-hearth type gasification furnace, comprising a furnace cover, a furnace cover seat, an outer furnace body, the inside of the furnace body and the heat preservation layer is set on the outer furnace body and the furnace body, the furnace body comprises a hearth, a hearth, a high temperature section and a base, a hearth and a second hearth is a split structure, the second upper hearth located in a cavity of the upper part of the hearth, and is coaxially mounted, it can improve the gasification of coal, the coal content, to save energy, reducing emission, and the split-type double-hearth gasification furnace is connected with a heating system, a bed system, which not only solves the problem that in winter, but also realizes the full use of the energy, reduces the waste of heat energy.
NOVELTY - The outlet pipe and the inlet pipe of the cyclone separator of the device, RY the molten salt pump. The utility model claims a fast molten salt pyrolysis biomass is connected with, the outlet pipe and the solid collector is cyclone separator, and the lower outlet of the cyclone separator is connected with a striking cone cracking reactor is connected, a cone cracking reactor and the biomass storage bin connected to, a condenser outlet is connected with a molten salt tank of the cracking reactor is connected with the liquid collector is connected with condenser, the outlet of the liquid collector are respectively by water channel is connected with the cracking gas storage tank and cracking gas, a cone on the upper part of the cracking reactor is connected with a motor. The beneficial effect of the utility model is: the utility model overcomes the heat energy utilization rate is low and the cost is high, and increases the yield of biomass fuel, realizes the continuous feeding and improve the use performance of the biomass in the production process.
NOVELTY - Microwave synthesizing diaryl amine compound, involves: carrying out condensation, isomerization and dehydration reaction of 3-shikimic acid methyl ester with aryl primary amine compound in the presence of an organic solvent, catalyst and micro-wave condition, which enables the occurrence of six-membered ring skeleton aromatization, and then cooling the reaction solution, adding the reaction liquid into saturated salt water, rapidly stirring, separating out solid, filtering, drying, re-crystallizing to obtain the 3-arylamino-4-hydroxybenzoate compounds.    USE - For microwave synthesizing diaryl amine compound (claimed).    ADVANTAGE - The method utilizes as a source material 3-shikimic acid methyl ester non-aromatic compound, which can be prepared by simple and convenient method; prepares diaryl amine compounds, which does not depend on fossil resources, which can realize the continuous development and utilization; and utilizes microwave method to provide short reaction time, simple and convenient operation, convenient post-treatment, high yield, clean and environment-friendly reaction, and low energy consumption.
NOVELTY - Producing bio-oil distillated fraction, comprises converting biomass in a conversion reactor containing a catalyst and is operated at 200-1000 degrees C to produce conversion reactor effluent vapor conversion products; condensing at least a portion of the vapor conversion products to form condensate comprising bio-oil and water; and fractionating a feed comprising at least a portion of the condensate by molecular distillation to form the bio-oil distillated fraction.    USE - The process is useful for producing bio-oil distillated fraction.    ADVANTAGE - The process provides fractionation of bio-oil by molecular distillation without subjecting the bio-oil to prolonged thermal stress.    DESCRIPTION OF DRAWING(S) - The figure shows schematic illustration of molecular distillation apparatus.    Molecular distillation apparatus (10)    Evaporator (102)    Evaporator surface (104)    Condenser (106)    Condenser surface (108)
NOVELTY - Producing diesel-like biofuel or an additive to diesel fuel having a chain length of 6-18C, comprises continuously or discontinuously performing a reaction in a liquid phase reactor of free fatty acids using acid supported catalyst, which is doped with a metal or a mixture of Group VIII metals.    USE - The method is useful for producing diesel-like biofuel or an additive to diesel fuel (claimed) by continuous, single-stage conversion of free fatty acids from renewable resources.    ADVANTAGE - The method allows rapid and economical production of diesel-like biofuel with high yield and less power consumption.
NOVELTY - The method involves selecting household garbage for garbage-recoverable recovery. The household garbage is dried, crushed and processed to reduce weight of the garbage. The garbage is provided to dechlorination treatment. Thermal cracking is carried out for the garbage using a cracking device for recycling oil gas mixture. The oil gas mixture mixed oil and combustible gas are fractionated. The oxygen content of the oxygen-enriched air is combusted to provide heat for metal smelting.    USE - Domestic garbage regeneration method.    ADVANTAGE - The method enables performing a dechlorination process so as to effectively inhibit dioxin in a process of forming. The method enables producing great economic benefit and environmental benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a domestic garbage regeneration method.
NOVELTY - The method involves processing biomass alcohol solution for heavy oil and hydrogen with hydro-refining catalyst, where the hydro-refining catalyst contains carrier and metal active component that includes VI group metal component or V group component. The VI group metal compound is chromium-containing compound, a key-containing compound, a tungsten compound and copper, silver, gold-containing compound. The VI metal component is selected from the group consisting of a Mo, tungsten and chromium.    USE - Method for refining hydrocarbon oil e.g. diesel oil and petrol oil, using biomass alcohol solution.    ADVANTAGE - The method enables improving hydro-refining effect, increasing light conversion rate, obtaining a product with high stability, and realizing high energy density and low content of water trace.
NOVELTY - Health-care tea comprises 30% of green tea, 20% of plantain herb, 20% of longhairy Antenoron herb, 10% of Chrysanthemum and 20% of radix puerariae as raw materials.    USE - The health care tea is useful for reducing uric acid (claimed) in a human body, promoting urination, expelling toxin, clearing and promoting microcirculation and treating diuresis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing health-care tea comprising heating the raw materials into an microwave at 120 degrees C and then drying for 15 minutes, crushing the heated materials into 40 meshes, and packing the product into a nylon ultrasonic triangular bag.
NOVELTY - An alcohol-based fuel comprises synergistic agent; ignition agent; cosolvent; corrosion inhibitors; metal deactivators; flame colorant; and anti-odor agent.    USE - An alcohol-based fuel.    ADVANTAGE - The alcohol-based fuel has high efficiency and energy-saving, is convenient to use, resists corrosion, safe and reliable, and is clean and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing an alcohol-based fuel comprises:    (A) providing 1-30 wt.% methanol, 0.01- 0.2 wt.% synergistic agent, 0.05-1 wt.% ignition accelerator, and 1-5 wt.% co- solvents;    (B) adding corrosion inhibitors, metal deactivators, colorants flame and odor agent, where corrosion inhibitor is added so that pH of material is 7-8; and    (C) adding metals deactivator agent, flame coloring agent, and anti-odor agent less than 0.0001 wt.% of total mass of methanol.
NOVELTY - Domestic waste solid fuel additive comprises component A comprising 50-150-mesh crushed food waste, sewage sludge, and livestock manure and organic waste, component B comprising 150-250-mesh crushed humic acid, 5-15 pts. wt. component C comprising 300-350-mesh black lead powder and iron oxide at 1:1-3 weight ratio, and 0.1-1.0 pt. wt. component D comprising 300-350-mesh calcium or magnesium hydroxide. The weight ratio of component A to component B is 1:0.2-0.3. The weight of components A and B is 100 pts. wt.    USE - Domestic waste solid fuel additive.    ADVANTAGE - The additive improves the formability, combustibility, and stability of solid fuel and effectively removes odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of domestic waste solid fuel additive comprising adding food waste, sewage sludge, livestock manure, and organic waste comprising paper, resin, metal, and waste glass into domestic waste stage processing device, magnetically removing the iron metal, crushing, adding the domestic waste solid fuel additive, drying, removing non-ferrous metal material, and cooling.
NOVELTY - Fertilizer comprises 0.005-0.3 wt.% pyrazosulfuron, and 0.1-5 wt.% mefenacet as active ingredient, 0.05-5 wt. pesticide, 78.7-98.995 wt.% carrier fertilizer, 0.2-3 wt.% solvent water as auxiliary agent, 0.1-1 wt.% stabilizer, 0.2-2 wt.% dispersant, 0.3-3 wt.% diluent and 0.05-2 wt.% safety agent.    USE - The fertilizer in granular form is useful for fertilizing, weeding and preventing rice borer and planthoppers in paddy field (claimed).    ADVANTAGE - The pyrazosulfuron mefenacet fertilizer is prepared by short process, stable and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, which involves (a) mixing pyrazosulfuron, mefenacet, stabilizer, dispersant, diluent and safety agent and crushing mixture to 5 mu icons or less mesh size, (b) mixing carrier fertilizer raw materials, granulating mixture, drying, cooling, and screening the mixture, and (c) mixing the mixtures obtained in step (a) and (b).
NOVELTY - Preparation of plant carbon plastic comprises putting plant raw materials into microwave vacuum tank, vacuumizing until vacuum degree of 0.02-0.001 MPa , microwave processing, pre-processing plant material, drying, carbonizing, calcining and cooling; and adding ultra-high molecular weight polyethylene and 100 pts. wt. modified polyvinyl chloride as base material in processing process, and adding 30-35 pts. wt. flame retardant, 3-12 pts. wt. toughening agent, 5-10 pts. wt. coupling agent, 2-5 pts. wt. antioxidant and 15-20 pts. wt. plant carbon of super smell molecular weight polyethylene.    USE - Method of preparation of plant carbon plastic (claimed).    ADVANTAGE - The plant carbon plastic is provided with excellent toughness, but also has high rigidity and hardness and good antistatic property and flame retardance.    DETAILED DESCRIPTION - Preparation of plant carbon plastic comprises putting plant raw materials into microwave vacuum tank, vacuumizing until vacuum degree of 0.02-0.001 MPa , microwave processing at 300-950 MHz for 3 minutes, pre-processing plant material, drying, carbonizing, calcining and cooling, controlling combustion speed of 5-15 degrees C/minute at 700-750 degrees C or 900-1000 degrees C for 40-80 minutes, increasing speed to 5-15 degrees C/minutes to 1000-1500 degrees C or 1600-1800 degrees C for 2-8 hours to obtain plant carbon; and adding ultra-high molecular weight polyethylene and 100 pts. wt. modified polyvinyl chloride as base material in processing process, and adding 30-35 pts. wt. flame retardant, 3-12 pts. wt. toughening agent, 5-10 pts. wt. coupling agent, 2-5 pts. wt. antioxidant and 15-20 pts. wt. plant carbon of super smell molecular weight polyethylene.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the preparation of plant carbon plastic.
NOVELTY - An organic composite fertilizer from poultry and livestock manure is prepared by mixing fresh pig manure and straw stalk or mushroom residue, adding into stainless steel fermentation tank, heating to 70-90 degrees C, adding bacterial strain, fermenting, heating while stirring, killing pathogenic bacteria and worm eggs, stopping heating, maintaining temperature at 70-90 degrees C using fermentation biological heat, taking out after 12-24 hours, accumulating gas to disperse moisture, adding trace elements, stirring, granulating, spraying functional microbial fertilizer on surface and packaging in bag.    USE - The method is useful for preparing organic composite fertilizer from poultry and livestock manure (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for stainless steel fermentation tank comprising processing pot main body (101) having stainless steel insulation layer. The processing pot main body is provided with axial exhaust suction fan (107), support (102) at the lower end, discharging port (105) at the bottom and stirrer (103) installed inside the body. The support has belt transmission device (106) at the lower part. The stirrer is connected with motor (104) and gearbox.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of stainless steel fermentation tank.    Processing pot main body (101)    Support (102)    Stirrer (103)    Motor (104)    Discharging port (105)    Belt transmission device (106)    Axial exhaust suction fan (107)
NOVELTY - Fuel composition comprises methanol (20-70 wt.%), liquid light hydrocarbon (20-65 wt.%), ethylene glycol (0.2-2 wt.%), butyl acetate (0.5-5 wt.%), oleic acid (0.2-8 wt.%), rubber swelling inhibitor (0.1-2 wt.%) and metal corrosion inhibitor (0.1-2 wt.%).    USE - The fuel composition is useful for a vehicle (claimed).    ADVANTAGE - The fuel composition can replace gasoline and is high in ratio, good in economical efficiency, high in applicability, good in usability and high in practicality, avoids the need to modify the engine, and does not corrode metal parts of automobile engines and rubber materials of oil storage systems and oil supply systems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fuel composition, comprising taking the above raw materials, successively adding ethylene glycol, butyl acetate, oleic acid, rubber swelling inhibitor and metal corrosion inhibitor into methanol, stirring it to uniformly mix to prepare improved methanol, adding the liquid lighter hydrocarbon into the improved methanol, stirring and mixing uniformly, and manufacturing a finished product of the vehicle fuel composition.
NOVELTY - Microbial liquid drip irrigation fertilizer is prepared by (a) weighing 1000 pts. wt. yeast abandoned liquid, (b) adding 4-5 pts. wt. sodium hypochlorite to the above-mentioned raw material, (c) stirring the mixture uniformly and sterilizing the mixture for 4-6 hours, (d) adding 0.5-1.5 pts. wt. Streptomyces microflavus strain as seed bacterium to the obtained mixture and (e) fermenting aerobically for 18-30 hours at 20-40 degrees C to obtain the fertilizer.    USE - The microbial liquid drip irrigation fertilizer is useful for improving wasteland and soil.    ADVANTAGE - The microbial irrigation fertilizer has large amount of organic materials, amino acids and trace elements, low production cost, is simple to apply and decomposes the materials which cannot be decomposed by existing yeasts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of microbial liquid drip irrigation fertilizer, which involves performing the above-mentioned steps (a)-(e).
NOVELTY - Production of dual acid chelate organic compound fertilizer involves using 10-20% green manure, 10-20% corn straw, 10-20% cake fertilizer, 10-20% animal manure, 8% distillers' grains, 15% pollution-free river mud, 9% turf, 3% organic fertilizer fermentation agent, 2% sterilizing deodorizer, 0.7% amino acid chelate ion, 0.3% amino acid chelate boron, 0.4% amino acid chelate copper, 0.3% amino acid chelate manganese, 0.4% amino acid chelate molybdenum, 0.3% humic acid chelate zinc, 0.3% humic acid chelate calcium and 0.3% humic acid chelate magnesium, as raw materials.    USE - Production of dual acid chelate organic compound fertilizer (claimed).    ADVANTAGE - The dual acid chelate organic compound fertilizer having long-term usagebility and efficiently regulated soil structure is produced. The abilities of plants to resist droughts, cold, adversities, continuous cropping, withering and yellowing, and root rot can be improved, and immune functions can be enhanced, using the dual acid chelate organic compound fertilizer.    DETAILED DESCRIPTION - Production of dual acid chelate organic compound fertilizer involves using 10-20% Green manure (mixture of sweet clover, Sesbania, alfalfa and Chinese trumpet creeper), 10-20% corn straw, 10-20% cake fertilizer (mixture of rapeseed cake, cottonseed cake, castor cake and tea seed cake), 10-20% animal manure (mixture of pig manure, cow dung and chicken manure in ratio of 5:4:1), 8% distillers' grains, 15% pollution-free river mud, 9% turf, 3% organic fertilizer fermentation agent, 2% sterilizing deodorizer, 0.7% amino acid chelate ion, 0.3% amino acid chelate boron, 0.4% amino acid chelate copper, 0.3% amino acid chelate manganese, 0.4% amino acid chelate molybdenum, 0.3% humic acid chelate zinc, 0.3% humic acid chelate calcium and 0.3% humic acid chelate magnesium, as raw materials.
NOVELTY - Biological straw fertilizer comprises nitrogen, phosphorus pentoxide, potassium oxide, organic matter of straws and biological synergist, where the nutrient content of nitrogen, phosphorus, potassium or organic matter of straws is not less than 1.6-2.5%, the biological synergist is prepared by fermenting bean straw, green bean straw, pea straw, rice straw, wheat straw, rape straw, peanut straw, hot pepper stalk, tomato stalk and dregs of commercial scale pharmaceutical factory.    USE - The biological straw fertilizer is useful in an agriculture or forestry field (claimed).    ADVANTAGE - The biological straw fertilizer has improved microorganism fertilizer effect and organic and inorganic fertilizer effect, preserves the ecological environment, and is innocuous and non poisonous fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biological straw fertilizer, comprising (1) fermenting the straw using a biological agent to obtain a semi-finished product, and (2) mixing and granulating the product via a full-automatic burdening computer to obtain the end product.
NOVELTY - Composite microbial fertilizer is obtained by raw materials comprising 200-500 pts. wt. yeast fermented powder residue, 200-500 pts. wt. organic fertilizer, 50-300 pts. wt. urea, 50-200 pts. wt. potassium sulfate, 50-200 pts. wt. ammonium dihydrogen phosphate, 30-50 pts. wt. clay and 10-20 pts. wt. composite microbial bactericide.    USE - The composite microbial fertilizer is useful for fixing nitrogen, increasing the nitrogen content in soil, and improving structure of the soil.    ADVANTAGE - The composite microbial fertilizer has phosphorus dissolution and potassium dissolution, and improves utilization rate of the chemical fertilizer, yield and quality of crops. The composite microbial fertilizer prevents diseases and insect pests naturally as metabolites produced by microbes.    DETAILED DESCRIPTION - Composite microbial fertilizer is obtained by raw materials comprising 200-500 pts. wt. yeast fermented powder residue, 200-500 pts. wt. organic fertilizer, 50-300 pts. wt. urea, 50-200 pts. wt. potassium sulfate, 50-200 pts. wt. ammonium dihydrogen phosphate, 30-50 pts. wt. clay and 10-20 pts. wt. composite microbial bactericide, where the composite microbial bactericide is obtained by fermenting Bacillus mucilaginosus (CICC23640), Bacillus megaterium (CICC21694), Bacillus cereus (CICC21687), Bacillus thuringiensis (CICC20565), Azotobacter chroococcum (ACCCI1104), powdery Pichia farinosa (ACCC20025) and Streptomyces microflavus (ACCC41134).
NOVELTY - Preparing terpin hydrate using continuous hydration process, comprises preparing acid water solution, pouring acid water solution and raw material into reaction kettle, heating and agitating the mixture, maintaining temperature of kettle, adding raw material and water into mixture, extracting the terpin hydrate and red oil to maintain the concentration of the acid water in the reaction kettle and the weight ratio of acid water and red oil to be stable, and discharging the terpin hydrate, red oil and acid water from the kettle.    USE - The method is useful for preparing terpin hydrate using continuous hydration process (claimed).    ADVANTAGE - The method is capable of preparing terpin hydrate with more than 30% of high production efficiency, achieving the yield of 100%, improving the yield of 10% in a simple, cost-effective and environmental-friendly manner.    DETAILED DESCRIPTION - Preparing terpin hydrate using continuously hydration process, comprises: (a) preparing the acid water solution; (b) pouring the acid water solution and raw material into a reaction kettle, and heating and agitating the mixture; (c) maintaining a temperature of the reaction kettle to be 25-35 degrees C for 5-15 hours; (d) continuously adding raw material and water into the obtained mixture, and continuously extracting the terpin hydrate and red oil to maintain the concentration of the acid water in the reaction kettle and the weight ratio of acid water and red oil to be stable; and (e) discharging the terpin hydrate, red oil and acid water from the kettle.
NOVELTY - Synthesizing piracetam comprises mixing the ethyl 4-chloro-n-butanoate, glycinamide hydrochloride, base or alcoholic organic solvent, heating and refluxing the mixture for 20-30 hours, hot filtering the mixture, decompressing evaporating the solvent from the mixture to obtain residue, recrystallizing, filtering and drying the residue, where the mole ratio of the ethyl 4-chloro-n-butanoate, glycinamide hydrochloride and base organic solvent is 1:1.1-1.8:1-2.    USE - The method is useful for synthesizing piracetam (claimed).    ADVANTAGE - The method is capable of synthesizing piracetam with short reaction step and mild reaction condition in a simple and environmental-friendly manner.
NOVELTY - Drying 1,3-di(hydroxymethyl)-5,5-dimethylhydantoin, comprises putting 5,5-dimethylhydantoin, formaldehyde and water into reactor, vacuum concentration, crystallizing and drying the mixture using low temperature heat pump type fluidized bed drier, evaporating liquid part of the medium, compressing the evaporated content into a condenser pipe, reducing temperature of the medium, discharging high temperature condensation heat of the medium into the drier, dehumidificating and transferring the wet medium into drier using drying material, drying the medium, and discharging.    USE - The method is useful for drying 1,3-di(hydroxymethyl)-5,5-dimethylhydantoin (claimed).    DETAILED DESCRIPTION - Drying 1,3-di(hydroxymethyl)-5,5-dimethylhydantoin, comprises putting 5,5-dimethylhydantoin, formaldehyde and water into a reactor for reaction, vacuum concentration, crystallizing and drying the mixture using a low temperature heat pump type fluidized bed drier, where: the drier comprises heat pump system comprising a compressor, an evaporator pipe, a condenser pipe and an expansion valve; the expansion valve comprises closed circulation loop filled with heat pump working medium; the heat pump working medium is connected with evaporator pipe to absorb heat of moisture cold air discharged from the drier, evaporating an liquid part of the medium using heating process, compressing the evaporated content into a condenser pipe using a compressor to carry out a condensation step and liquefaction step, reducing temperature of the medium, discharging high temperature condensation heat of the medium into the low-temperature drier and dehumidificating at 20-40 degrees C to obtain drying medium, and transferring the wet medium into drier using drying material and drying for 4-7 hours and discharging.
NOVELTY - A heterocyclic-substituted urea compound (I) is new.    USE - Heterocyclic-substituted urea compound is used as active framework, and organic synthesis intermediate of important pharmaceutical molecules.    ADVANTAGE - The heterocyclic-substituted urea compound is environmentally-friendly prepared with yield of 96%, under mild reaction condition, by a simple process.    DETAILED DESCRIPTION - A heterocyclic-substituted urea compound of formula (I) is new.    R1=halo or aryl;    R2=allyl, benzyl or group of formulae (i);    R3=t-butyl, cyclohexyl or aryl;    R4=methyl, methoxy or halo;and    X,Y'=not defined.    N.B. X,Y' is not defined. An INDEPENDENT CLAIM is included for preparation of heterocyclic-substituted urea compound (I).
NOVELTY - A trospium chloride is synthesized by putting alpha -tropine in high pressure reacting kettle, and using 1-1.5 wt.% of palladium/carbon (Pd/C) as catalyst for catalytic hydrogenating for removing methyl to obtain nortropine; putting nortropine, 1-4-dichlorobutane and triethylamine in reacting bottle to react to obtain chloridized (3- alpha -nortropine)-8-spiro-1-pyrrole ammonium salt; and taking diphenyl hydroxyacetyl chloride and chloridized-8-spiro-1-pyrrole ammonium salt to condense to obtain trospium chloride.    USE - Method for synthesizing trospium chloride (claimed).    ADVANTAGE - The method has short reacting step flows, high yield, and low production cos. It uses Pd/C catalytic hydrogenating to remove methyl, to recycle the catalyst and reduce its dosage. It further decreases pollution and provides for simple treating process after the reaction.    DETAILED DESCRIPTION - Synthesizing trospium chloride comprises:    (A) taking diphenyl hydroxyacetic acid and thionyl chloride in reacting bottle at a weight ratio of 1:2.6-3, and reacting to obtain diphenyl hydroxyacetyl chloride;    (B) putting alpha -tropine in high pressure reacting kettle, and using 1-1.5 wt.% of Pd/C as catalyst for catalytic hydrogenating for removing methyl to obtain nortropine;    (C) putting nortropine, 1-4-dichlorobutane and triethylamine in reacting bottle to react, a mole ratio of nortropine to 1,4-dichlorobutane being 3.3-3.6, and the dosage of triethylamine is 2.25-2.27 times the mole amount of nortropine, and reacting to obtain chloridized (3- alpha -nortropine)-8-spiro-1-pyrrole ammonium salt; and    (D) taking diphenyl hydroxyacetyl chloride and chloridized-8-spiro-1-pyrrole ammonium salt at a mole ratio of 1.1-1.2:1 to condense to obtain trospium chloride.
NOVELTY - Ergot alcohol is reacted in a methanol-sulfuric acid system under photocatalysis to prepare 10-( alpha )-methoxyl-light ergot alcohol. Methylation is carried out on the 10-( alpha )-methoxyl-light ergot alcohol and a methylated reagent in an aprotic polar solvent under the catalytic action of strong alkali to prepare 1-methyl-10-( alpha )-methyl-light ergot alcohol. Acylation reaction is carried out on the 1-methyl-10-( alpha )-methyl-light ergot alcohol and 5-bromine nicotinoyl halide in an aprotic hydrophobic solvent under the catalytic action of weak alkali to prepare the nicergoline.    USE - Preparation of nicergoline (claimed).    ADVANTAGE - The method enables preparation of economical, simple and environmentally-friendly preparation of high quality, low toxic nicergoline.
NOVELTY - A liquid carbon dioxide methanation catalyst comprises amphiphilic ionic liquid dispersed with metal active component existing in stable colloid state. The spherical metal active component having particle size of 0.5-20 nanometers comprises first metal active component and second metal active component at mol ratio of 10:0.1-2, where the first metal active component is nickel and the second metal active component is lanthanum, cerium, molybdenum, ruthenium, ytterbium, rhodium, palladium, platinum, potassium and/or magnesium.    USE - Liquid carbon dioxide methanation catalyst.    ADVANTAGE - The catalyst has low-temperature catalytic activity, methane selectivity and better thermal stability. The method is simple, feasible and has lower cost. The metal active component in the liquid carbon dioxide methanation catalyst has smaller particle size, narrower distribution and easier separation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of liquid carbon dioxide methanation catalyst comprising dispersing soluble salt of metal active component which is metal ion salt and amphiphilic ionic liquid in liquid medium at room temperature to obtain mixed solution, adjusting pH to 8-10, reacting and stirring for 1-3 hours, reducing with hydrogen at 100-200 degrees C and 0.1-4.0 MPa for 1-6 hours, centrifuging, filtering, washing and drying; and    (2) application of liquid carbon dioxide methanation catalyst for carbon dioxide methanation comprising adding liquid carbon dioxide methanation catalyst and solvent in reactor, controlling concentration of catalyst in reaction system at 0.0001-0.01 mol/L, infusing carbon dioxide and hydrogen, heating to 100-200 degrees C and catalyzing at 100-200 degrees C and 0.1-4.0 MPa for 1-6 hours.
NOVELTY - The eco-purification system has a to-be-treated water area which is divided into a microbe cultivating area and a sewage purification area. A water passage is arranged between the microbe cultivating area and the sewage purification area. The microbe cultivating area is divided into a first cultivating area (1) and a second cultivating area (2) which are communicated with each other. A biological packing reaction device (4) is arranged in each cultivating area.    USE - Water eco-purification system.    ADVANTAGE - Secondary pollution is avoided, since no chemical additive is used in the whole process and no sludge, garbage, odor and the like are generated. The operation and the management of the system are simple and convenient, and the energy consumption is low. The investment is low, and the benefits are high. The effluent quality is standard, the time is short, the efficiency is high, and the application range is wide. No special sewage construction work is required, the mounting time of the treatment equipment is only half a day, and the sewage can reach the standard within 7 to 20 days. Durability is realized, the service life of equipment is long, and the service life of main packing equipment can be longer than 50 years.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a purification method of water eco-purification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microorganism culture area.    First cultivating area (1)    Second cultivating area (2)    Biological packing reaction device (4)    Floss biological filler (42)    Micro-bubble aerator (43)
NOVELTY - A mixed refrigerant comprises component A, i.e. nitrogen, argon and/or neon; component B, i.e. tetrafluoromethane and/or methane; component C, i.e. methane, ethane, ethylene and/or monofluoromethane; component D, i.e. perfluoropropane, difluoromethane, propane, propylene and/or hexafluoropropylene; and component E, e.g. 1,1,1,2,2- pentafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, perfluorobutane, 1,1,2,2-tetrafluoroethyl methyl ether, 1,1,1,2,3,3- hexafluoropropane, 1,1,1,3,3-pentafluoropropane and 1,1,1,2,2,3,3,4,4-nonafluoro-4-iodo-butane.    USE - Mixed refrigerant.    ADVANTAGE - The refrigerant causes minimal greenhouse effect and does not depletes ozone layer.    DETAILED DESCRIPTION - A mixed refrigerant comprises 35-50 mol% component A, i.e. nitrogen, argon and/or neon; 10-35 mol% component B, i.e. tetrafluoromethane and/or methane; 5-20 mol% component C, i.e. methane, ethane, ethylene and/or monofluoromethane; 5-20 mol% component D, i.e. perfluoropropane, difluoromethane, propane, propylene and/or hexafluoropropylene; 5-25 mol% component E, i.e. 1,1,1,2,2- pentafluoropropane, 1,1,1,2,3,3,3-heptafluoropropane, perfluorobutane, 1,1,2,2-tetrafluoroethyl methyl ether, 1,1,1,2,3,3- hexafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,1,2,2, 3,3,4,4-nonafluoro-4-iodo-butane, 1,1,1,2,2,3,3-heptafluoropropane, 1,1,2,2,3,3,,4,4-octafluorocyclobutane, 1,1,1,2,3-pentafluoropropane, 1,1,2,2,3-pentafluoropropane, 1,1,1,2,3,4,4,4-octafluorocyclobutane and/or 1,1,1,2,2,3,3,4-octafluorocyclobutane.
NOVELTY - The device has frequency conversion heater whose end is connected with water tank (3) through water suction pump (4) and pipeline. The steam output end of frequency conversion heater is connected with drying oven (2) by the steam pipeline (5). The bottom of the drying oven is provided with vent holes. The steam pipeline is connected with water tank through vent holes. The output end of high frequency module (7) is connected to the electromagnetic heater (8).    USE - Device for treating food garbage through superheated steam.    ADVANTAGE - The food garbage in the drying oven is carbonized through the steam pipeline, so that food garbage treatment process can be performed safely, quickly and efficiently. The device can be controlled automatically and operated conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for treating food garbage through superheated steam.    Drying oven (2)    Water tank (3)    Water suction pump (4)    Steam pipeline (5)    High frequency module (7)    Electromagnetic heater (8)
NOVELTY - The system has feeder (20) whose outlet is connected to a biomass inlet of the preheater (30) by the spiral feeder (1a,1b). A biomass outlet of the preheater is connected to a biomass inlet of the pyrolysis furnace (10) by a pipe (9). A gas outlet of the pyrolysis furnace is connected to an inlet of the gas cyclone separator (40). A fuel feeding fan (90) is connected to a fuel inlet of the pyrolysis furnace. An outlet of flue gas cyclone separator is orderly connected to the tar catalytic cracking device (60), water cooler (70) and filter (80).    USE - Biomass pyrolysis device.    ADVANTAGE - The energy consumption of the system can be improved effectively and the efficiency of the system can be improved. The wastage of the resources can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass pyrolysis method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass pyrolysis device.    Spiral feeders (1a,1b)    Pipe (9)    Pyrolysis furnace (10)    Feeder (20)    Preheater (30)    Gas cyclone separator (40)    Catalytic cracking device (60)    Water cooler (70)    Filter (80)    Fuel feeding fan (90)
NOVELTY - Processing of pecan peel and bamboo shoot skin charcoal involves crushing pecan peel, bamboo shoot skin and bamboo and preparing pecan peel particles, bamboo shoot skin particles and bamboo particles, drying the pecan peel particles, bamboo shoot skin particles and bamboo particles until a moisture content reaches 7-10%, mixing the dried pecan peel particles, bamboo shoot skin particles and bamboo particles evenly, and then molding to firewood rods, and then carbonizing by carbonization furnace.    USE - Processing of pecan peel and bamboo shoot skin charcoal used for producing machine-made charcoal (all claimed).    ADVANTAGE - The method efficiently and economically provides machine-made charcoal having high strength, carbon content and calorific value, without causing pollution to environment.
NOVELTY - Ethanol-water azeotropic distillation separation method involves performing methyl tert-butyl ether (MTBE) direct circulating process, MTBE flash evaporation circulating process and three-column distillation circulating process using MTBE (gasoline additive) as entrainer, to obtain automotive fuel. Concentrating column is used to conduct preliminary concentration process of raw material ethanol, and azeotropic rectification method is performed to conduct concentration process of obtained ethanol. Water phase after separating ethanol from azeotropic rectification column is reused.    USE - Ethanol-water azeotropic distillation separation method during preparation of automotive fuel ethanol (claimed).    ADVANTAGE - The method efficiently provides ethanol product having reduced content of water, with reduced contents of ethanol and entrainer in wastewater, and energy consumption.    DETAILED DESCRIPTION - Ethanol-water azeotropic distillation separation method involves performing methyl tert-butyl ether (MTBE) direct circulating process, MTBE flash evaporation circulating process and three-column distillation circulating process using MTBE (gasoline additive) as entrainer, to obtain ethanol product as automotive fuel. Concentrating column is used to conduct preliminary concentration process of raw material ethanol, and azeotropic rectification method is performed to conduct concentration process of obtained ethanol. The entrainer can be reused. Water phase after separating ethanol from azeotropic rectification column is reused. The separation of ordinary ethanol-water mixture and separation of bioethanol is carried out by the method, without performing separation of entrainer MTBE from ethanol. An INDEPENDENT CLAIM is included for preparation of automotive fuel ethanol from water-ethanol mixture.
NOVELTY - Phase stabilizer comprises alkyleneoxide compound.    USE - The phase stabilizer is useful for in a methanol gasoline (claimed).    ADVANTAGE - The phase stabilizer effectively solves a problem that the methanol gasoline is easy to demix after absorbing water, and the methanol and the gasoline are separated at low temperature while a proportion of the methanol is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a methanol gasoline comprising phase stabilizer (5-15 wt.%), gasoline (30-70 wt.%), methanol (20-60 wt.%), corrosion inhibitor (0.5-5 wt.%) and detergent (0.5-5 wt.%); and    (2) preparing the methanol gasoline, comprising dissolving the corrosion inhibitor and the detergent, adding the phase stabilizer after dissolving, uniformly stirring to obtain the mixture, sealing to store for later use, adding methanol and gasoline in a stirrer, and stirring fully and slowly adding the mixture to obtain a finished liquid fuel product.
NOVELTY - Preparing biomass grain fuel comprises processing gastric content, processing adipose tissue leftover, mixing raw material with auxiliary material, granulating the mixed balk, harmlessly processing it at high temperature, and cooling and dewatering the grain.    USE - The method is useful for preparing biomass grain fuel using cattle and sheep gastric content and leftover adipose tissue (claimed).    ADVANTAGE - The method is capable of economically preparing the biomass grain fuel with high applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the biofuel.
NOVELTY - A biochemical denitrification device comprises water distributing system with circulating and mixing functions, three-phase separator and anoxic sludge layer. The upper part of the system is provided with three-phase separator and middle part is provided with anoxic sludge layer.    USE - Device used for processing biochemical denitrification of high nitrogen organic wastewater.    ADVANTAGE - The device removes total nitrogen and reduces processing cost.
NOVELTY - Cortex moutan radicis bark total flavone extract comprises 40-95 wt.% cortex moutan radicis bark total flavone.    USE - Cortex moutan radicis bark total flavone extract.    ADVANTAGE - The method has simple technique, low energy consumption, no pollution, good environmental benefit, and high total flavone content, and uses solvent i.e. ethanol and water, which can be recycled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cortex moutan radicis bark total flavone extract comprising taking dry cortex moutan radicis peel as raw material, extracting with water or ethanol containing water, concentrating the extracting liquid to obtain extract, adding water or ethanol containing water to dissolve the extract, centrifuging to obtain supernatant, removing the impurities, loading the supernatant into polyamide resin column, eluting with water or hydrous ethanol, removing the impurities, eluting with ethanol or hydrous ethanol, collecting the eluate, and concentrating and drying the eluate to obtain cortex moutan radicis bark total flavone extract.
NOVELTY - Device comprises a drying chamber and a crushing chamber. The walls of the drying chamber are made of toughened transparent glass. The drying chamber is set with a sludge recycling spreading device. A geothermal coil pipe is connected with a ground source heat pump. A hot air nozzle is connected with a heat exchanger. The crushing chamber is provided with a coarse crusher and a fine crusher, which are mutually connected with each other. Material outlets of the drying chamber and crushing chamber are connected with a stirrer, which is connected with a punch through a spiral conveying device.    USE - The device is useful for preparing fuel rod by mixing papermaking sludge and riddling of household rubbish (claimed).    ADVANTAGE - The device: is capable of recycling papermaking sludge and rubbish; effectively recycles waste resource; protects the environment; has low manufacturing cost; has simple structure and convenient operation; and is suitable for large-scale industrial production.
NOVELTY - Improving biogas yield through plant fermentation, involves cloning lignin peroxidase gene and manganese peroxidase gene, laccase gene and endoglucanase enzyme gene, dextran exonuclease gene and beta glucosidase gene, constructing Escherichia coli-B.subtilis shuttle plasmid comprising the above-mentioned genes, transforming B.subtilis by the plasmid to obtain engineered bacteria, and applying B.subtilis engineered bacteria and natural biogas fermentative microorganisms in a pretreating process of plant raw material fermentation.    USE - The method is useful for improving biogas yield through plant fermentation (claimed).    ADVANTAGE - The method improves the plant raw material utilization rate and the biogas yield. In the method, that lignin and celluloses left in the plant fermentation for the biogas can be hydrolyzed, and development of an industry which uses plant fermentation for the biogas is promoted.    DETAILED DESCRIPTION - Method for improving biogas yield through plant fermentation, involves cloning lignin peroxidase gene and manganese peroxidase gene of white rot fungi, laccase gene of Bacillus subtilis and endoglucanase enzyme gene, dextran exonuclease gene and beta glucosidase gene of Trichoderma, constructing Escherichia coli-B.subtilis shuttle plasmid comprising the above-mentioned genes, transforming B.subtilis by the plasmid to obtain engineered bacteria, and applying B.subtilis engineered bacteria and natural biogas fermentative microorganisms in a pretreating process of plant raw material fermentation for biogas, where the B.subtilis engineered bacteria are applied in biogas production using the fermentative plant.
NOVELTY - This utility model claims a biomass thermal cracking furnace, comprising a hearth, a feeding pipe and is provided with a stirring blade of the rotating shaft, a feeding pipe extends into the hearth, the hearth, the feeding pipe is provided with a material storing platform, a rotating shaft of the stirring blade on the feeding pipe in the hearth opening to the space between the storage platform. The beneficial effect of the utility model is that, to optimize the structure of biomass material pyrolysis furnace, storage plate in the hearth, the bottom of the hearth swept by rotating a stirring blade, the stirring blade of the rotating speed can be controlled, so that the bottom of the hearth material can be set according to technical requirements, at the same time, provided with a sight glass, a valve, an auxiliary speed control for feeding, the flexibility and the controllability of the biomass thermal cracking furnace.
NOVELTY - Biomass solid fuel power, belonging to the field of mechanical equipment technology field. The structure is as follows: comprising a base, a motor, a storage bin, a motor is connected with the taper of cone, the cone is connected with cone, cone is sleeved on the main shaft, the lower end of the main shaft by a bearing and is fixedly connected with the main shaft sleeve and the cone connected to bottom of the water tank, the upper half of the main shaft is located in the storage bin, the end is provided with a rolling disk on the main shaft, the main shaft of the two sides of the weld is set with rolling pressure cavity is provided with a porous disc at the bottom of the storage bin. The device uses the cone transmission way, cone tank device replace the existing worm wheel and worm transmission mode, has stable transmission, transmission power loss is small. Cone movement which drives the main shaft, the main shaft high, solves the problem that the centrifugal force generated by the main shaft from abrasion problem, greatly improves the mechanical life of the device. Rolling shaping link does not need to heat and save energy.
NOVELTY - The utility model claims a solid heat carrier moving bed biomass pyrolysis device, comprising ball heating furnace, heat carrier biomass ball dosing machine, moving the pyrolysis material layer, moving-bed pyrolyzing furnace body, biomass storage bin, wherein the heat transfer medium is inert solid ball, solid heat carrier of heat transfer method is radiation heat transfer and heat transfer. This utility model is main ball of radiant heat transfer and heat transfer, is far higher than the pyrolysis of indirect heat transfer method, the utility model avoids pyrolyzed coal gas mixed gas, the coal quality is greatly improved, this utility model uses moving bed for pyrolysis, the pyrolysis gas as fly ash content is greatly reduced, the power consumption is obviously reduced; tar dust content is essentially property is reduced, operation cost is reduced, the utility model is new type gas cylinder carrying vehicle ball circulating method, ball heat removing at least part of radiation outside the whole return to be reused, and the heat transfer medium, the gas with high temperature discharged pyrolysis method, system heat efficiency is greatly improved.
NOVELTY - The utility model is the one kind of biomass gas industrial furnace system, belonging to the biomass gasification heat utilization technology field, wherein a feeding port is installed on the side wall of the gasification furnace, a gasification furnace outlet is set with cyclone dust collector, a cyclone dust remover through pipeline is respectively connected with the combustion chamber, the nozzle and the industrial furnace, the air pipe is installed on the uniform pressure chamber, and the pressure chamber are tangent, the utility model is the biomass gas industrial furnace system is provided with high efficiency, stable operation, no pollution, solving the biomass heat utilization technology is difficult to use in the technical problem of industrial furnace system.
NOVELTY - This utility model belongs to the field of new biomass pyrolysis system technology field, especially relates to a kind of three-phase reactor biomass pyrolysis system and a working method thereof. This utility model system is composed of a fast fluidized bed oxidizing furnace, a cyclone separator, a flue gas pipe, a material returning valve, a bubbling fluidized bed furnace, a material returning valve, a second cyclone separator, a CO2 pipe, the third material returning valve, a rotary pyrolyzing furnace, gas outlet and hot packing auger, the utility model is a fast fluidized bed oxidizing furnace, reactor design a bubbling fluidized bed calcining furnace and rotary pyrolyzing furnace, the reaction temperature of each reactor and so on working condition parameter only independent with each other are associated with each other, wherein the main influence factor is that the material of the double chemical chain selection and ratio, the utility model is new-type CO2 from zero to discharge positive discharge, gas of H2 content is more than 80%, reduces the heat loss of the biomass energy, at the same time prevent the semi-coke to the environment pollution.
NOVELTY - This utility model claims a gasification furnace cover, especially a new-type gasification furnace, comprising a gasification furnace body, the gasification furnace main body is provided with a furnace cover, the furnace cover and the furnace body shell is matched with the shell of the furnace cover and the furnace body outer shell are respectively provided with a refractory material layer, a furnace cover is provided with a furnace top upper edge matched with the groove, the groove is provided with a heat-resisting cushion contacted with the furnace top. This utility model has reasonable and compact structure, the manufacturing is simple, the cost is low, the efficiency is high, minitype motor cooling system of kitchen widely used, the user health is ensured, the manufacturer also brings high economic benefit.
NOVELTY - Preparation of 2-methyl benzothiazole derivative involves adding acetic anhydride and 2-aminothiophenol halide in a glacial acetic acid reaction system at 80-200 degrees C, cooling to room temperature, filtering, cooling the filtrate to 5 degrees C, slowly dripping 1-20 %mass sodium hydroxide aqueous solution, adjusting pH value to 7 plus minus 0.5, extracting by organic solvent, distilling to remove organic solvent, and obtaining 2-methyl benzothiazole derivative.    USE - Preparation of 2-methyl benzothiazole derivative (claimed).    ADVANTAGE - The method enables easy, environmentally-friendly and economical preparation of 2-methyl benzothiazole derivative by a simple process with reduced energy consumption.    DETAILED DESCRIPTION - Preparation of 2-methyl benzothiazole derivative involves adding acetic anhydride and 2-aminothiophenol halide in a glacial acetic acid reaction system at 80-200 degrees C, cooling to room temperature, filtering, cooling the filtrate to 5 degrees C, slowly dripping 1-20 %mass sodium hydroxide aqueous solution, adjusting pH value to 7 plus minus 0.5, extracting by organic solvent, distilling to remove organic solvent, and obtaining 2-methyl benzothiazole derivative. The -aminothiophenol halide is of formula (I)-(IV).    X=Cl or Br.
NOVELTY - The furnace has a biomass raw material storage groove fixed on an upper part of a furnace body. The biomass raw material storage groove is equipped with a feeding port sealing cover and a discharging port. The upper part of the furnace body is provided with a guide cylinder, a first air inlet and a fuel gas inlet. A middle part of the furnace body is provided with a second level air inlet. A lower part of the middle furnace body is provided with a fire bar. A lower part furnace body is provided with an opening and a fuel gas outlet.    USE - Multi-stage down-sucking type biomass gasification furnace.    ADVANTAGE - The furnace improves conversion efficiency and quality of the biomass fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a multi-stage down-sucking type biomass gasification furnace.
NOVELTY - This utility model belongs to the power station boiler firing new method technology field, especially relates to a kind of double-fluidized bed biomass pyrolysis and ignition system and a working method thereof. The system is composed of a reaction device and a boiler ignition device, reaction device and material returning valve, a burner, a pyrolyzer flue gas separator, the first and the second material returning valve, gas separator, hot packing and high temperature fuel gas fan, a boiler ignition device comprises a boiler burner, a hearth and a gas igniter, the utility model uses the high temperature biomass gas enter the hearth through boiler at the lowest layer lighter gas combustion, fuel gas combustion and the combustion temperature of the pulverized coal igniting a burner of the pulverized coal, so as to achieve the purpose of ignition and pressure rising of boiler. This utility model can provide high temperature fuel gas for large capacity power plant pulverized coal boiler firing stage to replace the traditional ignition manner, which solves the problem that the energy.
NOVELTY - The utility model claims a kind of used for a biomass carbon gas cogeneration system of parallel heat storage type high temperature coal gas heat-carrying medium heating system, this utility model comprises a heat accumulating chamber, a low temperature section reversing valve, a reversing valve and a high temperature area wall cooling smoke gas combustion furnace, and each device is connected with the corresponding pipelines of the gas, a heat storage chamber of a parallel heat-accumulating chamber, which are parallel heat storage chamber A and parallel heat-accumulating chamber. A parallel regenerator heat exchanger heating gas, the coal gas reaches the high temperature in the combustion furnace, in order to lower the furnace wall temperature, protection lining material, a cold gas fume wall for protection. The technical advantage of the utility model is: it can produce the high temperature coal gas is more than 800, a high temperature coal gas as heat-carrying medium solves the problem that the heat-carrying gas is reducing gas quality. A heat storage mode heat exchanger heating gas, is featured with high safety, material resisting high temperature and low cost heat exchanger. In addition, cold wall gas combustion furnace using cold gas fume-protecting technology, the furnace lining work condition is good, the radiating furnace body, furnace lining;
NOVELTY - This utility model belongs to biomass thermal conversion technology field, especially relates to a kind of a air cylinder is a cylinder of water vapour gasification device for preparing synthesis gas by a process. Comprising a material blending device (1), a feeding port (2), an observation hole (3), a cylinder (4), an outer heat preservation cylinder (5), an inner cylinder (6), steam distribution device (7), an air distribution port (8), a device (9), an inner cylinder draught fan (10), a temperature measuring device (11), an outer cylinder draught fan (12), the ash discharging device (13), (14), a waste heat boiler (15), a carbon dioxide absorption tower (16). This utility model using a cylinder air gasification, a cylinder steam gasification the energy self-supply in the cylinder from a catalytic reforming, steam gasification to obtain hydrogen and carbon monoxide volume content of synthesis gas is 85-90%.
NOVELTY - This utility model belongs to the technical field of biomass energy, referring to a kind of thermal cracking of biomass boiler, comprising a cracking reaction kettle, a heating furnace, a fuel gas combustion device, a heat conducting oil pipeline device, a steam generating device for heat conducting oil, synthesis gas condensing device, synthesis gas non-device, wherein the biomass thermal cracking reacting kettle can be set on the heat insulation furnace, the heat insulating furnace wall is provided with a heating device, a heat conducting oil pipe device, a heat conducting oil pipe device passes is connected to a generating device using heat conducting oil as heat-insulating furnace, synthesis gas condensing device and the synthesis gas non-filter device with thermal cracking reacting kettle. This utility model claims a thermal cracking of biomass boiler, at the same time, the decomposition of the biomass material, fully uses the heat generated by a reaction material in the reaction kettle to generate the biomass carbon is a kind of theftproof device for merchandise, a sales profit, synthesis gas generated by the condensing liquor also can be recycled, cracking process discharge the redundant heat is also a kind of civil or industrial use.
NOVELTY - Preparing soil base comprises (1) fermenting organic biomass material and then compositing, (2) fermenting straw and other biomass material at 50-60 degrees C, (3) mixing the obtained products in step (1) and (2) and then drying, (4) adding lime and nitrification inhibitor with the mixture to adjust he water content to 15-20%, (5) preparing an inorganic matrix, (6) mixing the obtained products in step (4) and (5), and then (7) granulating, checking and packaging.    USE - The method is useful for preparing soil base (claimed), where the soil base is useful for preventing and treating multiple diseases, weed, underground pests and nematodes and soil acidification.    ADVANTAGE - The method prepares the soil base in an eco-friendly and cost effective manner with low toxicity. The soil base avoids continuous cropping obstacle phenomenon.
NOVELTY - This utility model claims a kind of high-tower urea formaldehyde sustained release compound fertilizer production device, belonging to the fertilizer manufacturing equipment technology field. The tower comprises a tower, the main tower is equipped with a material conveying device, a groove and the lower end of the spraying device is connected with the hoisting machine and urea-formaldehyde reaction pump, is connected with the inlet of the urea melting groove, urea melting tank and adhesive urea solution storage tank is connected with inlet of the adhesive urea solution storage tank and formaldehyde steam buffer groove, formaldehyde steam buffer groove, formaldehyde and formaldehyde rectifier storage tank are connected in turn, the material conveying device of the urine buffer slot is urea-formaldehyde reaction pump is connected with the urine buffer tank, a solid material heater are connected with the feed port of the mixing tank, and the output end of the mixing tank is connected with the spraying device, the lower end of the tower is set with a hopper, the lower end outlet of the hopper is connected with a material conveying device. This utility model adopts said structure, it has convenient to configure, saved investment, low cost, saving energy and reducing consumption.
NOVELTY - Composting appliance comprises at least a first container capable of containing compostable materials and an odor sensor configured to sense malodor emitted from the first container.    USE - The appliance is useful for composting waste in landfills, where the compost is useful as an economical source of plant food.    ADVANTAGE - The appliance ensures continuous and rapid composting of waste in landfills by increasing the efficiency of active phase to lower the time of the curing phase, and is ready-to-use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of composting comprising: (a) providing a home composter comprising (i) the first container, (ii) the odor sensor, (iii) a perfume dispenser capable of dispensing a perfume composition, where the odor sensor and the perfume dispenser are configured to be in electrical communication, and (iv) a vial containing the perfume composition, where the vial is configured such that the perfume dispenser is in fluid communication with the perfume composition contained in the vial; (b) containing compostable materials in the first container; (c) composting the compostable materials contained in the first container; (d) emitting malodor in airspace from the compostable materials contained in the first container; (e) sensing malodor emitted from the first container in the airspace using the odor sensor; and (f) dispensing the perfume composition contained in the vial in response to the sensed malodor emitted from the first container.
NOVELTY - B100 biofuel composition comprises combustible hydrocarbons from biological source feedstocks, and an alkyl phenol amine aldehyde condensate to improve the stability of the fuel.    USE - The B100 biofuel composition is useful in unmodified diesel engine vehicles.    ADVANTAGE - The B100 biofuel composition is cost-effective and eco-friendly, has synergistically improved oxidative stability, high flash point for safe handling and quality, good lubricity and reduced emissions of lower particulate matter, carbon oxides and unburned hydrocarbons, and inhibits residue formation and discoloration.
NOVELTY - Device for processing of moist organic substrate into gaseous energy carriers, comprises sequentially arranged dehydrating device, gas generator, wet scrubber and power-generating device, where between output of scrubber on liquid flow and sump, the anaerobic bio-filter is provided, whose output on gas is connected to a power-generating device.    USE - The device is useful for processing of moist organic substrate into gaseous energy carriers (claimed).    DETAILED DESCRIPTION - Device for processing of moist organic substrate into gaseous energy carriers, comprises sequentially arranged dehydrating device, gas generator, wet scrubber and power-generating device, where between output of scrubber on liquid flow and sump, the anaerobic bio-filter is provided, whose output on gas is connected to a power-generating device, where output on gas is connected with power-generating device sequentially connected with dryer, installed between output of dehydrating device by solid fraction and shaft of gas generator, and also with heat exchanger device, installed between aerobic hydrolysis device and blasting device of gas generator, input on liquid flow is additionally connected with liquid output of dehydrating device, and before dehydrating device the aerobic hydrolysis device is placed, where output of aerobic hydrolysis device on gas is connected with furnace of gas generator.
NOVELTY - A biomass alcoholysis method involves contacting an alcohol solvent with biomass under closed conditions in the presence of a biomass liquefaction catalyst, where boiling point of the alcohol solvent is not less than temperature of the alcohol solvent in contact with the biomass at normal pressure.    USE - Method for alcoholysis of biomass.    ADVANTAGE - The method enables alcoholysis of biomass with high biomass liquefaction rate, and the biomass alcoholysis oil has high calorific value, low viscosity and low acid value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biomass alcoholysis oil which involves contacting biomass with an alcohol solution to obtain a liquefied product. A light component and heavy component is separated from the obtained product. A steam extraction is performed on the light component to separate the alcohol solvent, and the obtained product is extracted with the heavy component to obtain a mixture under a hydrogenation refining condition. The mixture and hydrocarbon is heated with a hydro-refining catalyst in the biomass to carry out an alcoholysis method.
NOVELTY - Recycling agricultural and forestry waste pyrolysis and gasification catalyst comprises impregnating waste raw material in catalyst aqueous solution, carrying out solid-liquid separation to obtain impregnated liquid, recycling the liquid, drying the impregnated waste raw material, pyrolyzing to obtain gas-, liquid- and solid products, collecting the gas product by a gas collecting cabinet, allowing the liquid product to stand for separation to obtain wood vinegar and tar product, and recycling the solid product, which is biomass carbon containing catalytic element as a catalyst and pyrolyzing.    USE - The method is useful for recycling agricultural and forestry waste pyrolysis and gasification catalyst (claimed).    ADVANTAGE - The method recycles the catalyst residual solution and solid product as catalyst with high efficiency and low cost.    DETAILED DESCRIPTION - Recycling agricultural and forestry waste pyrolysis and gasification catalyst comprises mixing waste raw material with catalyst aqueous solution in a stirring reactor, stirring and impregnating, carrying out solid-liquid separation to obtain impregnated liquid, recycling the impregnated liquid into a mixing reactor, drying the impregnated agricultural and forestry waste raw material, carrying out pyrolysis in a pyrolysis reactor to obtain gas product, liquid product and solid product, collecting the gas product by a gas collecting cabinet, allowing the liquid product to stand to carry out separation to obtain wood vinegar and tar product, recycling the solid product, which is biomass carbon containing catalytic element as a catalyst, and carrying out pyrolysis of the agricultural and forestry waste raw material in a batch wise manner or after impregnation drying of the raw materials.
NOVELTY - Tobacco straw materials remaining after harvest are chosen, and tobacco straw root soil and debris are cleaned. The tobacco straws are arranged neatly and dried to a water content of less than 15%, and tobacco straws are collected and transported to a repository for storage for more than 20 days. The water content is continuously reduced to less than 8%. The tobacco straws are crushed to a powder of less than 5 mm and bagged. The tobacco straw powder is then dehydrated to a water content of less than 7% and carbonized in a carbonizing furnace to obtain biochar.    USE - Preparation of biochar using tobacco straws (claimed).    ADVANTAGE - The method improves the use efficiency of waste resources and economical benefits of tobacco straws, and provides stable carbon conversion. More than 20% of carbon dioxide emission caused by decomposition of tobacco straws is reduced, thus reducing environmental pollution. The method is also beneficial for improvement of soil quality of farmlands, and saves cost of agricultural production.
NOVELTY - The method involves polishing (S10) graphite block in a fuel cell separator automatically. The graphite block is automatically transported with a transfer apparatus and the plane of the graphite block is polished (S12) using a polisher. The graphite block in a graphite plate is cut (S13) by using a cutter. The plane of each transferred graphite plate is polished (S15) with the polisher. The semi-finished product is dipped in the dipping solution and is washed in a washing tub. The moisture is removed from the surface of the semi-finished product.    USE - Method for manufacturing a fuel cell separator (Claimed) using porous graphite.    ADVANTAGE - The method involves polishing a graphite block in a fuel cell separator automatically, thus enables stabilizing the manufacturing process of the fuel-cell separator, improves the quality of the fuel cell separator, ensures mass production, reduces the personnel cost, and also reduces the manufacturing time of the fuel cell separator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for manufacturing fuel-cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a fuel cell separator manufacturing method. (Drawing includes non-English language text).    Polishing graphite block in a fuel cell separator (S10)    Polishing plane of the graphite block (S12)    Cutting graphite block using a cutter (S13)    Transferring the nibbling by the transfer apparatus (S14)    Polishing plane of each transferred graphite plate (S15)
NOVELTY - Chromatographic separation of gamma -aminobutyric acid (GABA) and glutamic acid comprises filtering glutamic acid-containing GABA through membrane filter, centrifuging to clarify, filtering through plate and frame filter, concentrating through heat concentration or membrane concentration to obtain 1-90 wt.% aqueous solution, adjusting pH to 2-11, filling special chromatographic media at 0-100 degrees C into chromatographic column, eluting, collecting eluates and residual liquid, separating GABA and glutamic acid, and decoloring GABA.    USE - Method for chromatographic separation of gamma-aminobutyric acid and glutamic acid (claimed).    ADVANTAGE - The method is simple and environment-friendly and has low cost and high separating degree.
NOVELTY - A secondary biomass solid fuel preparation method involves mixing a de-inking sludge with less than or equal to 30% water, and introducing additives and ingredients of biomass into a pellet or briquette, where the de-inking sludge comprises cellulose fibers, printing inks, adhesives and 10-30% fillers, and calorific value of the water is 8-12 MJ/kg.    USE - Method for preparing secondary biomass solid fuel from waste paper industry.
NOVELTY - A perfluoroethyl isopropyl ketone is prepared by mixing hexafluoropropylene dimer and fluoro-4-methyl-2-alkene or perfluoro-2-methyl-2-pentene, and subjecting mixture to epoxidation reaction.    USE - Method of preparing a perfluoroethyl isopropyl ketone (claimed).    ADVANTAGE - The method has mild reaction condition and high conversion rate, can be applied to industrial production, and is simple, easy, safe, low cost and environment-friendly.
NOVELTY - A biomass discontinuous carbonization and heat generating method involves heating biomass to temperature of 500-550 degrees C. The biomass is thermally decomposed into flammable volatile fractions, pyrolysis gas and coal. The pyrolysis gases are escaped through holes in a combustion chamber and burnt. Coal is cooled in a tray and accumulated in containers for industrial application.    USE - Method for performing discontinuous carbonization of biomass and generating heat.
NOVELTY - The utility model claims a biomass energy utilization device, especially refers to a kind of biomass carbonizing system, mainly comprising a charging, a feeding hopper, a carbonization furnace, a dust remover, a dust collecting water seal tank, a condenser, an exhaust pipe, a spiral feeding machine, a spiral discharging machine, a chimney, wherein the carbonization furnace at the upper part of the right side is equipped with a spiral feeding machine, a spiral discharging machine at the bottom of the carbonization furnace is provided with a fan connected with the air inlet pipe, an air inlet adjusting valve is set on carbonization furnace right side and four layers of wind, a carbonization furnace at the upper part of the right side is provided with an exhaust three-way pipe, the carbonization furnace shell made of steel plate, the furnace is provided with a fire-resisting layer, a heat preservation layer, and the lower end is provided with a discharging hopper and an annular cooling water tank. The advantages are as follows: the energy density is low, can not be directly burning the biomass is converted to heat a high fixed carbon, so the income of farmers.
NOVELTY - This utility model claims a kind of sludge and household garbage to prepare biomass fuel of the complete set of equipment, wherein it is as follows: in a stepped arrangement in turn connected with a disintegrator, magnetic separation device, a spiral conveyer, a roller sieve, crusher, a spiral conveyer, a stirring crusher, a third spiral conveyer, the fourth screw conveyor, an electronic device, a fine crushing forming machine, a drier and a gas processing device. This utility model uses sludge and household garbage by complete equipment, adding additive, to prepare biomass fuel forming device without dehydration treatment, a drying at low temperature, reduce the running cost of the maximum extent and saves energy consumption to realize sludge and household garbage volume reduction decrement, harmless and resource.
NOVELTY - This utility model claims a kind of vehicular livestock manure concentrated processing device, wherein it comprises a vehicle platform, a distribution device, a crushing device, a stirring device and the extrusion forming device, wherein the transmission and distribution device, a crushing device, a stirring device and the extrusion forming device are installed on the platform, the inlet of the crushing device of the power transmission and distribution device, the outlet is connected with the mixing device is a crushing device, a mixing outlet is connected with extrusion forming device. This utility new type mobile device, which is convenient for the livestock manure is processing, which avoids the livestock excrement in transportation process, a transmission and distribution device, a crushing device, a stirring device and the extrusion forming device, the livestock manure and coal and solidified together, stirring and extrusion forming, high heat value of the fuel.
NOVELTY - This utility model claims a kind of livestock manure concentrated-processing system, wherein it comprises a transmission and distribution device, a crushing device, a stirring device and the extrusion forming device, inlet of the bottom end outlet of the crushing device of the power transmission and distribution device, the outlet is connected with the mixing device for crushing device, stirring outlet connected with extrusion forming device. According to transmission and distribution device for lifting belt conveyor. This utility model is a transmission and distribution device, a crushing device, a stirring device and the extrusion forming device, the livestock manure and coal and solidified together, stirring and extrusion forming, high heat value of the fuel.
NOVELTY - The utility model claims a combined gas and cooling the water electrolysis hydrogen preparing electrolysis bath device, comprising a cooling plate assembly, a membrane insulating sealing pad component, nickel grid auxiliary electrode, end electrode plate, the negative electrode plate, and the positive end pressure plate, pressure plate, cooling the bipolar plate assembly, a membrane insulating sealing pad component, nickel grid auxiliary electrode, end electrode plate, the negative electrode plate, and the positive end pressure plate, pressing plate combination into the electrolytic groove main body by a screw fastening piece of the main body is provided with a fan, the fin pipe type condenser, gas-liquid separator and a gas-liquid separator, a fan is connected to the upper end of a W-shaped fin pipe type condenser, upper left W-shaped fin pipe type condenser is connected with the gas-liquid separator, a right W-shaped fin pipe type condenser is connected with the gas-liquid separator, the lower electrolytic cell main body is provided with a hydrogen side Y-type liquid collecting pipe, oxygen side Y-type liquid collecting pipe, liquid pipe and oxygen through liquid pipe and a hydrogen side. It has good cooling effect, low manufacturing cost, small occupied area and space is small.
NOVELTY - The device has a steam pipeline (12) fixed with a heat exchanger (21) that is arranged in a heating and dehydrating area of a furnace body. A combustion zone of the furnace body is provided with a hearth (15). A spraying mechanism is connected with the furnace body of a fire extinguishing region. A heating exchanger is connected with a steam pipe (38) and a cooling water pipe (40). A chain grate part (4) is fixed with the furnace body, which is connected with a carbon box body (39). A water heating sleeve box body (14) is fixed with a hot water inlet pipe (33).    USE - Biomass combustion device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass combustion device.    Chain grate part (4)    Steam pipeline (12)    Water heating sleeve box body (14)    Hearth (15)    Heat exchanger (21)    Hot water inlet pipe (33)    Steam pipe (38)    Carbon box body (39)    Cooling water pipe (40)
NOVELTY - A kind of animal integrated septic tank by marsh gas, comprising a front end septic cavity, cavity, three-cylinder septic end cavity, wherein the front end cavity, three-cylinder septic chamber septic end cavity is combined structure, the septic chamber is mounted on the front end cavity and the three-cylinder septic tail end cavity and a bolt, the front end of the cavity and a three-cylinder septic end cavity are respectively provided with a sealed, septic and septic cavity and tail end cavity and septic cavity is provided with an access opening at the front end, the upper part of the end cover is provided with a top cover, the front end of the support frame is provided with a fixed cavity and three-cylinder septic end bottom of the cavity, the tail end cavity is provided with a septic outlet. This utility model has simple structure, convenient construction, good sealing property can be a volume of a cavity of the septic tank integrally by increasing the number of the septic chamber is a telescopic structure, it is convenient to transport, it can stretch septic cavity, a single septic chamber capacity, reduce economic cost in the using process.
NOVELTY - A kind of trash and biomass waste special processing gasification furnace, mainly comprising a furnace body (1), a gas generating chamber (2), a turntable body (3) and tank (4), wherein the furnace body (1) of the outer layer is provided with a cooling water layer (12), the inner layer is provided with a refractory material layer (14), the bottom is provided with a fire grate (16), and a device is provided with a spraying port (18), a furnace body (1) is a thermal decomposition chamber (17), a furnace body (1) of the lower part of the coal gas generating chamber (2) and the air outlet (21), and the bottom is further provided with a rotating plate body (3) and tank (4). This utility model has compact and simple structure, reliable work, low cost, easy to popularize and use and simple maintenance and repair.
NOVELTY - A method of effectively neutralizing lime waste involves carrying out anaerobic treatment of wastewater containing organic matter, where the anaerobic treatment is conducted by collecting biological gas, subjecting the collected gas to biogas combustion, collecting gas produced by burning lime waste, subjecting the collected gas produced by burning lime waste to post-combustion treatment, and effectively neutralizing lime waste.    USE - For effectively neutralizing lime waste (claimed).    ADVANTAGE - The method can effectively reduce the pH value of the lime waste, has good effect of neutralizing lime waste, makes full use of biogas combustion rest heat, and forms product that is more stable. The method is capable of effectively reducing the pH value of the lime waste.
NOVELTY - The method involves reducing certain amount of nitrogen in coal bed gas in coal bed methane content to lower limit explosion limit. Certain amount of nitrogen is compressed to 0.5 to 0.4 MPa. Pressure swing adsorption is utilized to remove nitrogen and oxygen in the coal bed gas by vacuum from adsorption phase to obtain 30% of methane gas. Volume of the coal bed methane content is about 8 to 20%. Amount of nitrogen-containing methane volume content is added in the coal bed gas.    USE - Method for concentrating methane in low-concentration coal bed methane in a mine by utilizing pressure swing adsorption process.    ADVANTAGE - The method enables increasing the methane content to about greater than 30% and ensuring better environment benefit and economic benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for concentrating methane in low-concentration coal bed methane in a mine by utilizing pressure swing adsorption process. '(Drawing includes non-English language text)'
NOVELTY - Use of mulberry for planting Dendrobium candidum comprising carrying out uniform felling to collect mulberry leaf, drying in dark place, cutting, adding raw materials including 25% of tung peel, 10% of sheep manure, 60% of Camellia and 5% of fertilizer element, composting the mixture, fermenting in a culture medium, piling up for 15 days, turning the mixture once during fermentation period, again fermenting for 35 days, decomposing fermented organic fertilizer, is claimed.    USE - The mulberry is useful as fertilizer for planting Dendrobium candidum (claimed).    ADVANTAGE - The mulberry fertilizer ensures low production cost, high production efficiency and nutrient content, reduced resource waste, effectively realizes Dendrobium candidum cultivation with a length of 50-60 cm and thick stem of 8-10 cm after 24 months of planting, improved germination rate of 80%, and yield per unit area of 1600 kg.    DETAILED DESCRIPTION - Use of mulberry for planting Dendrobium candidum comprising carrying out uniform felling to collect mulberry leaf, drying in dark place, cutting using a machine with a length of 5-8 cm, adding raw materials including 25% of tung peel, 10% of sheep manure, 60% of Camellia and 5% of fertilizer element, where tung peel contains 3-5% of potassium, sheep manure contains 0.23%-0.46% of potassium and 0.66% of nitrogen content and 30% of organic matter, and fertilizer element contains 1.3% of nitrogen, 0.17% of phosphorus and 1.13% of potassium, composting the mixture, fermenting in a culture medium, piling up for 15 days, turning the mixture once during fermentation period, again fermenting for 35 days, decomposing fermented organic fertilizer, is claimed.
NOVELTY - Greening base comprises stone slag field soil, droppings, straw and charcoal powder.    USE - Used as greening base.    ADVANTAGE - The greening base has soil antiscour ability, low water loss and soil erosion damage, can beautify environment and reduce slag accumulation, improve mine ecological environment and recycle utilization of land resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the greening base comprising (1) crushing stone field residue soil by 10-20 mm sieve, crushing livestock manure and straw by 5 mm meshes sieve, weighing the stone extraction field slag soil, droppings, straw and charcoal powder, (2) mixing straw with droppings and decomposition agent to obtain a mixture, and (3) mixing the stone slag field soil and charcoal powder with the obtained mixture.
NOVELTY - This utility model claims a controllable inner and outer double-circulating high-efficient anaerobic reactor is composed of anaerobic reactor and anaerobic reactor from bottom to top in turn is provided with a water inlet pipe, a primary reaction zone, the first level three phase separator, a secondary reaction zone, a level three phase separator, a water outlet pipe, a gas-liquid separator, an exhaust pipe, a lifting pipe and is set on the first grade lift pipe can control circulating reflux pump, wherein it is provided with a gas-liquid separator is divided into two areas, the first level three phase separator of the lifting tube and the second level three phase separator of the lifting pipe is separating chamber and the gas-liquid of two regions in the gas-liquid separator, a return pipe and a level lift pipe are respectively provided with a control circulating reflux pump. The internal and external circulation anaerobic reactor of this kind of structure is provided with controllability, so as to improve the adaptability of the reactor, the reactor, starting domestication time. Partition is set at the same time of the gas-liquid separating chamber and a primary tri-phase separating area section area provided with improves the separation effect of biogas and sludge, removing the material liquid aluminium short circuit and so on, improves the reaction efficiency and production rate.
NOVELTY - This utility model claims a kind of combined coal pyrolysis gasifying a combustible gas, comprising a pyrolysis reactor, cracking reactor, a catalyst collecting groove, the collecting groove, the pyrolysis gas chromatograph and vapour generator, a cracking reactor component is located in the pyrolysis reactor, cracking reactor is provided with a catalyst bed layer, a cracking reactor is provided with a second pipe, a gas chromatograph and a steam generator are connected with the cracking reactor, the catalyst a collecting groove for collecting the pyrolysis coke as the catalyst carrier surface loaded active component as catalyst bed layer, pyrolysis collecting groove for collecting the pyrolysis, cracking reactor via a pipeline. This utility model can produce the pyrolysis of tar and pyrolysis gas generated by pyrolysis to obtain the high efficiency hydrogen-rich fuel gas with high concentration, the deactivated catalyst and the remained pyrolysis the water vapour in the hydrogen-rich gas produced by gasification at the same time can be recycled metal active component of the catalyst, the coal pyrolysis of a plurality of joint.
NOVELTY - Vapour esterification deacidification and protective device, the device is one kind of biological diesel oil comprises feeding heater, esterification kettle, a gas-liquid separating tower. Feeding heater adopts tubular heat exchanger, one end is connected with methanol feeding pump, one end is connected with the bottom of the esterification kettle methanol gasification, the esterification kettle through a bottom heater. Esterification kettle is provided with a jacket heating system, kettle top with a stirring device, the kettle is equipped with oil raw material and catalyst, gas phase methanol peak by gas-liquid separating tower kettle to methanol rectification device. Gas-liquid separating tower uses filler tower, the gas phase methanol containing acid liquid and acid catalyst droplets pass through a gas-liquid separator, a liquid catch the esterification kettle along flow tower, the gas phase methanol and separating tower through a gas-liquid enter into methanol rectification system. The utility model capable of accelerating reaction, protection device, reduce the corrosion.
NOVELTY - This utility model claims a kind of biological diesel oil ester exchange reaction of outer circulation stirring reaction device, comprising a methanol alkali tank and reaction kettle, a condenser, a pump circulation system. Ester exchange reaction kettle is provided with a jacket heating, with stirring, kettle top is provided with a condenser, a circulating pump inlet, a raw material inlet, bottom with a discharge port, a circulating pump interface. Methanol gas to mass transfer and reaction process waste grease, methanol alkali ester exchange into the reaction kettle by a feeding pump, a reaction kettle jacket for heating, a reinforcing oil by pump circulation system passes through the kettle top condenser. This utility model aims at grease and methanol polarity difference is not dissolved, by the external pump circulation and reinforcing mass transfer reinforcing and methanol raw material, accelerate the ester exchange reaction.
NOVELTY - The utility model claims a sludge compost odour automatic collecting device. It comprises turner (6), and is fixed on the machine (6) of the upper part (5), (5) plate (4) and the branch air duct provided with a (3), (3) is connected with the air valve (2) and (1), it further comprises an air valve automatic sensing control system, comprising a bracket (10) is set on the fermentation groove wall (13) of the infrared sensor (11), a baffle plate bracket is fixed on the machine (6) of the upper part (9), and a baffle plate bracket (9) is fixed on the baffle plate (12), the infrared sensor (11) and the air valve (2) of the power supply switch. This utility model realizes the starting of the wind pipe how synchronously moved with the turner is a problem to realize high efficiency of ozone, and of collecting network information automatically.
NOVELTY - This utility model claims a kind of straw gas furnace. The straw gas furnace comprises gasification tube, a combustion cylinder and combustion, the combustion net is set in the combustion chamber, the burning net is provided with a combustion space and the combustion cylinder, the inner part of the gasification cylinder is provided with an air grid, the straw is practical in the mesh enclosure, the upper part of the centre is provided with a cylindrical space, the lower end of the combustion chamber is connected to the cylindrical space of a connector, the connector is set at the lower end in the cylindrical space of the connector is provided with a sealing ring sleeved on the outer sidewall, a gasification tube on the side wall is provided with an air inlet and an ignition hole. This utility model claims a kind of simple structure, high heat utilization rate of straw gas stove.
NOVELTY - A gasoline additive contains 3-5% of methanol, a node agent and gasoline, where the octane number of methanol is 110; where the gasoline additive when test in a vehicle road condition test, obviously influence power property of gasoline, and increases the octane number of methanol and reduces the exhaust pollution.    USE - As gasoline additive for power engine (claimed).    ADVANTAGE - The gasoline additive increases the octane number of methanol and reduces the exhaust pollution.
NOVELTY - Extracting pyrethrin from insect-killing pixel chrysanthemum, involves drying, crushing and breaking wall of the insect-killing pixel chrysanthemum, performing multi-stage counter-current extraction pulse, carrying out counter-current thin film evaporation and a negative pressure absorbing and filtering separation, and rectifying and purifying.    USE - For extracting pyrethrin from insect-killing pixel chrysanthemum (claimed)    ADVANTAGE - The method greatly improves the yield of pyrethrin in an industrial scale; provides continuous production; is environmentally-friendly; has low production cost; and has good economic benefit and social benefit.
NOVELTY - Extracting puerarin involves: taking kudzu root as raw material, drying it, then crushing it into particles having 0.5-2 mm diameter, and then carrying out supercritical carbon dioxide extraction, and finally extracting carbon dioxide enriched with target substance to carry out primary and secondary decompressing and separating and analyzing the effective substance.    USE - For extracting puerarin (claimed).    ADVANTAGE - The method provides puerarin having more than 99% purity; consists of automatic equipment control; is easy to operate; doesn't provide solvent residue; is simple; saves energy and labor cost; and is safe and environment-friendly.
NOVELTY - The utility model claims a kind of organic matter fermentation tank, comprising a front side is provided with a box door, wherein the fermentation in the fermentation tank body is provided with a bearing organic substance bearing plate, the bearing plate and the bottom plate of the box body for forming the first air flow passage; the lower end of the fermentation and the side wall of the box is provided with a blower, the blower outlet is connected with the first air flow channel, the device can be provided with high-efficient oxygen supplying system for garbage fermentation, and manufacturing cost of the device is low, the technical requirement is low.
NOVELTY - A method of manufacturing local flavor fermented fertilizer involves: prior to inoculating heating Bacillus coagulans in molasses alcohol waste mash at high temperature (more than 90 degrees C); discharging the waste mash liquid and cooling to less than 45 degrees C, and then inoculating the obtain alkali Bacillus strain and Alcaligenes faecalis to dual fermentation; adding glue peptone Bacillus and Bacillus megaterium and fermenting to obtain safe ozone-free organic fertilizer of waste mash bacteria liquid.    USE - In manufacturing local flavor fermented fertilizer (claimed).    ADVANTAGE - The method provides safe ozone-free organic fertilizer that improves soil, increases active roots, reduces the plant diseases and insect pests.
NOVELTY - A method of manufacturing liquid fertilizer for seaweed involves: adding seaweed residue to water according to the weight of ratio of 1:1-5 and stirring to obtain mixture (m1); adjusting pH of the mixture to 6.8-7.2 using concentrated hydrochloric acid; adding 0.05-0.5 wt.% of complex enzyme into the mixture and carrying out enzymolysis at 30-40 degrees C for 20-28 hours to obtain enzymolysis liquid; and centrifuging the enzymolysis liquid to obtain sodium alginate liquid fertilizer comprising 0.2-1 wt.% of alginic acid, and 5-15 wt.% of organic material.    USE - In manufacturing liquid fertilizer such as sodium alginate liquid fertilizer for seaweed (claimed).    ADVANTAGE - The method of manufacturing liquid fertilizer, uses seaweed residue and solves environment pollution problem, is economical; provides sodium alginate liquid fertilizer that can improves the vegetable crop photosynthetic rate, and promote the growth of vegetable, and improves yield of vegetables.
NOVELTY - Mixing organic gasoline comprises mixing 20-40 vol.% low-carbon mixed alcohol, 40 vol.% N-methyl aniline, 40 vol.% o-toluidine, 0.005-0.01 vol.% gasoline detergent, 0.0001-0.01 vol.% metal deactivator and 0.001-0.01 vol.% corrosion inhibitor and stirring under room temperature and normal pressure condition.    USE - The method is useful for mixing organic gasoline (claimed).    ADVANTAGE - The method is simple, economical and environmental friendly; utilizes small dosage of materials; and suitable in small oil refinery industries.
NOVELTY - A machine for processing kitchen garbage, comprises a crushing device (9), a dehydrating device, a box body, a feeding opening, a stirring device (4), a biochemical treatment device (6), an exhaust device (1), discharging device (8), where the upper box body is provided with an electric control device, air device, a temperature control device and a feeding opening, where the box body is provided with a stirring device, a crushing device and a biochemical treatment device.    USE - In processing kitchen garbage for making fertilizer (claimed) including nitrogen fertilizer, phosphate fertilizer.    ADVANTAGE - The machine for processing kitchen garbage, is simple in structure, reduces garbage of 1/10 to 1/15 of original volume; provides solid slag which is rich in nitrogen and phosphorus element; and kills harmful bacteria.    DESCRIPTION OF DRAWING(S) - The figure shows a machine for processing kitchen garbage.    Exhaust device (1)    Stirring device (4)    Biochemical treatment device (6)    Discharging device (8)    Crushing device (9)
NOVELTY - Manufacturing fertilizer for sugar-cane using molasses fermentation liquor involves fertilizer granulating stages, adding each ton of fertilizer with 50-600 kg of water content is 30 -60% of molasses fermentation liquid, evenly spraying concentrated solution on compound fertilizer granulating disk or rotary drum, pelleting the concentrated solution.    USE - For manufacturing fertilizer for sugar-cane (claimed).    ADVANTAGE - In the traditional technique for producing compound fertilizer by using molasses alcohol zymotic fluid and replace with water, is derived from sugar cane molasses ferment liquid in reducing sugar cane, which not only makes full use of effective nitrogen-phosphorus-potassium nutrient of molasses ferment liquid, organic matter, amino acid, humic acid and trace element, sugarcane plant nutrient imbalance and unbalance the soil fertility, but also can solve the pollution problem of molasses ferment liquid to the environment, the molasses ferment liquid waste is changed into treasure, the cane sugar increase production, promoting sugar industry industrial sustainable development.
NOVELTY - Preparing soil culture matrix involves mixing 60-65% sand, 15-20% grass carbon, 6-8% perlite, 7-9% rapeseed cake, and 3-7% phosphate fertilizer, crushing, rotten for 10-12 days, diluting 50-60 times in 40% formaldehyde liquid spraying base, stirring, placing for 24-36 hours, and transferring to the greenhouse.    USE - For preparing soil culture matrix (claimed) for replacing soil environment.    ADVANTAGE - The method prepares soil culture matrix that provides mineral nutrition, water and gas environment; is wide and low price; reduces planting cost; prevents the heat and water loss; and improves more than 25% planting sedge.
NOVELTY - Preparing selenium-enriched fermented biological organic fertilizer, involves mixing the selenium-enriched edible fungi culture medium and crushed livestock manure to get the basic material, adding ferment fungus curved to the base material in the ferment, fermenting to obtain mixture, adding nitrogen, phosphorus, potassium, humic acid and trace elements to obtained mixture, mixing them uniformly, crushing, sieving to obtain a powder product; and pelletizing the powder product to obtain granular product.    USE - For preparing selenium-enriched fermented biological organic fertilizer (claimed).    ADVANTAGE - The method is simple, low cost, green and environment friendly.
NOVELTY - Pig litter base manure comprises 23 pts. wt.% rice hull, 12 pts. wt.% corn cob, 18 pts. wt.% plant ash, 25 pts. wt.% sawdust, 8 pts. wt.% wheat straw, 14 pts. wt.% fly ash.    USE - As pig litter base manure used as crops organic fertilizer (claimed).    ADVANTAGE - The pig litter base manure has strong absorbing and deodorizing effect, at the same time, degrade quickly under the action of pig manure, can be directly used as crops organic fertilizer.
NOVELTY - Litter pad material in form of press pad material is composed of pig manure together with several components, where main raw materials include 19% carbonized rice hull, 23% corn core, 18% plant ash, 23% sawdust, 13% wheat straw, and 4% fly ash. For producing the litter pad material; raw materials according to proportion are uniformly mixed, and then twice a day in morning and evening are sprinkled in barn.    USE - As litter pad material formed from pig manure, which is useful as organic fertilizer for crops (claimed) and for feeding multiple domestic animals.    ADVANTAGE - The pressed litter pad material including pig manure solves problems associated with degradation and deodorization of pig manure and purifies pig growth environment. The pressed litter pad material can be directly used as organic fertilizer for crops i.e. can be used in ecological cycle. The formulation is not only scientific, reasonable, and balanced, but also has strong water absorption and deodorization effect, such that pig manure can degrade quickly, can be directly used as crops organic fertilizer and is also suitable for feeding multiple domestic animals.
NOVELTY - Pig pad material comprises 21% carbonized rice hull, 18% corn core, 25% plant ash, 13% sawdust, 7% wheat straw, 16% fly ash as raw material.    USE - As pig pad material (claimed) as crops organic fertilizer, ecological cycle; as food of multilivestock.    ADVANTAGE - The pad material is used as pig manure and has fast degradation, deodorizies and purifies pig growth environment and can be directly used as crops organic fertilizer, ecological cycle use; is reasonable, is in balanced matching, has strong absorbing and deodorizing effect, at the same time, degradation is fast under the effect of the pig manure.
NOVELTY - Preparing composite microorganism liquid fertilizer involves adding dicyandiamide (DCD) and/or 3,4-dimethylpyrazolphosphate (DMPP), where the adding amount is 0.25-10 mass%, if need to add a kind of is 1:1 according to the proportion of weight, at the same time adding 0.3%-0.5% polyaspartic acid (PASP) and 0.2-0.6% soluble agent.    USE - For preparing composite microorganism liquid fertilizer (claimed).    ADVANTAGE - The method has simple technique, without increasing the three wastes discharge, is energy saving and environmental-friendly and reduces emission.
NOVELTY - Charcoal generator for stoves, is claimed.    USE - The charcoal generator is useful for stoves e.g. tiled stoves, garage stoves, wood and coal stoves, in industrial boiler systems e.g. gas-brown and hard coal power plants, cogeneration plants and waste incineration plants, and in wood chipping stoves, wood pellets stoves and metal casting stoves; and carbon bound by the process is useful for reducing the greenhouse gas e.g. carbon dioxide in the atmosphere (all claimed).    ADVANTAGE - The charcoal generator enables inexpensive charcoal production that makes use of the heat generated by the combusted wood, and the produced charcoal has no residual moisture content, which glows quickly and uniformly without producing smoke.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the coal produced from the charcoal generator.    DESCRIPTION OF DRAWING(S) - The drawings 1 and 2 show schematic representations of the charcoal generator.    Container (1)    Lid (2)    Bore (3)    Mountings (4)
NOVELTY - Generating biogas (12) from biomass (14), comprises providing biomass in a biogas plant and adding at least one methanogenic microorganism to the biomass, where at least one methanogenic microorganism is of the order Methanosarcinales.    USE - The method is useful for generating biogas from biomass.    ADVANTAGE - The method ensures optimized production of biogas and produces high proportion of methane.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process flow of the method for generating biogas.    Biogas (12)    Biomass (14)    First container space (42)    Second container space (44)    Temperature (48)
NOVELTY - Invention relates to a method of processing fat and fat-containing biomass. The method can be used in producing fuel and intermediate products for organic synthesis. The method is carried out via simultaneous exposure to ionising radiation and temperature of fatty material at normal or low pressure in a fluidised bed to obtain commercially valuable radiolysis products, which are a fuel (primarily diesel fuel) and intermediate products for organic synthesis. The material is exposed to an electron beam with energy of 0.1-8 MeV with dose rate higher than 0.05 kGy/s while heating below the dry distillation (pyrolysis) onset temperature. Alkanising the starting mass, use of catalysts and/or ultrasound can be additional controlling factors depending on composition of the starting material.    USE - Chemistry.    ADVANTAGE - High degree of recycling material and output of valuable fractions of fuel hydrocarbons and intermediate products for heavy organic synthesis.6 cl, 2 tbl, 10 ex
NOVELTY - The system (1) has a treated-water discharge unit (23) that discharges treated-water outside by using organic waste water overflowing from upper end of anaerobic-treatment space (33) as a treated water. An anaerobic-treatment tank (12) is provided with retention-of-gas space where the biogas is located above anaerobic-treatment space, and emitted and floated up in anaerobic-treatment space is stored temporarily. A retention-of-gas space pressure reduction unit (P6) is provided to reduce the pressure of retention-of-gas space.    USE - Anaerobic-treatment system.    ADVANTAGE - The outflow of granule sludge can be suppressed, and also the increase of ground contact area of the whole anaerobic-treatment system can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic-treatment system.    Anaerobic-treatment system (1)    Anaerobic-treatment tank (12)    Treated-water discharge unit (23)    Anaerobic-treatment space (33)    Retention-of-gas space pressure reduction unit (P6)
NOVELTY - The system (1) has a fuel vapor supply line (L6) whose one end is connected to respective end of fuel-supply line and the other end is connected to modifier (11). A purge unit supplies purge gas (G3) to fuel vapor supply line. A temperature detection unit (52) detects temperature of fuel in fuel vapor supply line and vapor (W1). A sensor (53) detects excess-air-ratio with respect to fuel and vapor. A control unit (51) controls supply units to stop vapor and fuel supplies and purge unit to supply the purge gas to fuel vapor supply line when excess-air-ratio is at specific range.    USE - Solid oxide fuel cell system.    ADVANTAGE - The control unit controls supply units to stop vapor and fuel supplies and purge unit to supply the purge gas to fuel vapor supply line when excess-air-ratio is at specific range, so that the oxygen is prevented from touching the ruthenium which comprises a catalyst under high temperature and the catalyst is suppressed from carrying out oxidation volatilization.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of fuel cell system.    Fuel cell system (1)    Modifier (11)    Control unit (51)    Temperature detection unit (52)    Sensor (53)    Purge gas (G3)    Fuel vapor supply line (L6)    Vapor (W1)
NOVELTY - The apparatus has a water tub (12) that is formed at lower portion of a waste gas influx unit (11). A rotary shaft (21) of a motor (2) is horizontally mounted inside a process bath (1). A drainpipe (13) is provided in lower portion of the water tub, and is provided with an opening/closing valve (131). An exhaust pipe (6) is provided for exhausting the process gas introduced into a gas induced space (33) of a cylinder rotation filter section (3). A jet water spout (4) is provided to circulate the jet water to the outside through spray holes (41).    USE - Wet-type apparatus for treating waste gas such as toxic gas, acidic gas, combustible gas such as silane, disilane gas, arsine gas, phosphine gas, and environmental gas such as sulfur hexafluoride, nitrogen trifluoride, fluorine gas, ethane gas, and propene gas, used in semiconductor production factory.    ADVANTAGE - The dust included in the waste gas can be removed, by circulating the jet water. The throughput performance of the waste gas treatment gas can be improved. The waste gas can be consecutively processed while the generation of the effluent is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the waste gas treatment apparatus.    Process bath (1)    Motor (2)    Cylinder rotation filter section (3)    Jet water spout (4)    Exhaust pipe (6)    Waste gas influx unit (11)    Water tub (12)    Drainpipe (13)    Rotary shaft (21)    Gas induced space (33)    Spray hole (41)    Opening/closing valve (131)
NOVELTY - Preparing fuel based on hydrogen and carbon dioxide resulting from combustion of carbonaceous fuel, comprises employing a catalyst with a carrier structure for the catalytically active substances comprising ceramic and/or zeolite.    USE - The method is useful for preparing the fuel based on hydrogen and carbon dioxide.    ADVANTAGE - The method is efficient with respect to utilizing heat (a waste product used by power plants) as a resource, and with regard to improving the carbon dioxide-balance in a case of high carbon dioxide-emissions in energy generation plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the catalyst for producing the fuel from carbon dioxide and hydrogen, comprising zeolites as a carrier material for the catalytically active substances.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a system for preparing the fuel, the drawing includes non English language text.
NOVELTY - Method (M1) of producing a biodiesel, comprises: providing a microalga; disrupting the microalga to obtain a disrupted microalga; and mixing the disrupted microalga directly with a catalyst, alcohol and co-solvent to produce the biodiesel.    USE - The method is useful for producing a biodiesel.    ADVANTAGE - The method saves the cost of process of microalgal oil extraction; and directly utilizes the wet microalgae as the raw material for producing the biodiesel, which omits the process of drying the wet microalgae, thus saving the relevant cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (M2) for producing a biodiesel, comprising: providing the microalga; disrupting the microalga to obtain the disrupted microalga; and performing a transesterification in which the disrupted microalga is directly used as a reacting material to produce the biodiesel;    (2) a method (M3) for producing a biodiesel, comprising: providing a biomass having an oil; obtaining a crude mixture from the biomass; and performing a transesterification in which the crude mixture is used as a reacting material to produce the biodiesel; and    (3) a biodiesel mixture comprising: the biodiesel produced by the above methods; and the residue.
NOVELTY - The apparatus has cathode (502) whose one end is connected to a voltage drop load resistance (401) and the other end is connected to an anode (501). A diode array (203) is provided for rectifying alternate current (AC) power source (201) applied from outside of load resistance (301). An electrolysis current generating unit (300) is provided for outputting impulse current to charge and discharge direct current (DC) outputted from one end of the load resistance and inserting output to an electrolyte that mixes graphene and carbon nano tube with potassium hydroxide solution.    USE - Apparatus for producing hydrogen from electrolysis of water by electrical superposition circuit.    ADVANTAGE - The supply of the electrode exchange electric current density can be facilitated. Since the electron mobility is high according to coat graphene on the cathode, the over voltage of the hydrogen generation cathode can be decreased. The electric conductance the electric power of the carbon nano tube can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the hydrogen production apparatus.    AC power source (201)    Diode array (203)    Electrolysis current generating unit (300)    Load resistance (301)    Voltage drop load resistance (401)    Cathode (502)
NOVELTY - The modular fuel cell system has power modules (12) which are arranged in a row on a base (20). A fuel processing module (16) and a power conditioning module (18) are arranged on ends of row on base. Each power module is provided with input/output cabinet (14) with fuel cell stacks located in hot box (13). The power modules are electrically and fluidly connected to fuel processing and power conditioning modules through base. The base is formed of pre-cast concrete, geopolymer or steel. The inner portion and outer portion of main portion are made of plastic.    USE - Modular fuel cell system.    ADVANTAGE - The modular fuel cell system enclosure is arranged, such that modular fuel cell system can be serviced easily. The routinely or high serviced components can be placed in single module, so as to reduce amount of servicing time required for the service person. The power modules, fuel processing module and power conditioning module can be easily serviced without opening the other module cabinets and without servicing the other modules. The pre-cast base is provided in sections, so that the overall weight of the structures to be transported, manipulated, and installed can be reduced efficiently. The cost of polymer outer portion can be reduced by reducing manual labor and material needed for construction of the door. The service life of the filters can be extended, so that the secondary servicing costs due to service personnel visits and filter consumables can be reduced effectively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an adsorption bed assembly; and    (2) a method for making modular fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows an isometric view of the modular fuel cell system.    Power modules (12)    Hot box (13)    Input/output cabinet (14)    Fuel processing modules (16)    Power conditioning module (18)    Base (20)
NOVELTY - The hydrogen generating apparatus (100) has a modifier (3) which generates a hydrogen-containing-gas by a reforming reaction using a raw material. A hydro-desulfurization device (2) removes a sulfur compound in the raw material. A downgradient (7) is formed in a recycle flow path through which the hydrogen-containing-gas added to the raw material before flowing into the hydro-desulfurization device flows. A drainage channel (8) drains the condensed water condensed in the recycle flow path formed with the downgradient.    USE - Hydrogen generating apparatus for use in fuel cell system (claimed).    ADVANTAGE - Since the condensed water generated in the recycle flow path is drained through the drainage channel, the need of separate condenser in the hydrogen generating apparatus can be avoided. Thus, the structure of the hydrogen generating apparatus can be simplified in compact form and the manufacturing cost of the hydrogen generating apparatus can be reduced. Since the water seal is provided in the drainage channel, the leakage of the hydrogen-containing-gas outside through the drainage channel can be prevented and the hydrogen-containing-gas can be stably sent to the hydro-desulfurization device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydro-desulfurization device (2)    Modifier (3)    Downgradient (7)    Drainage channel (8)    Hydrogen generating apparatus (100)
NOVELTY - The hydrogen combustion is carried out in presence of a magnesium catalyst (13) which is mixture of magnesium chips and powder, in an enclosure with orifices for discharging gases and carbon and/or sulfur atoms, to form magnesium oxide and water. The magnesium catalyst is regenerated in same enclosure, by introducing extra hydrogen, to obtain water and heat.    USE - Process for obtaining thermal energy (claimed).    ADVANTAGE - The method enables reliable and efficient formation of thermal energy with controlled hydrogen combustion rate, without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for installation for combustion of hydrogen in admixture with carbon oxides, nitrogen oxides and/or sulfur oxides.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the installation for combustion of hydrogen in admixture with carbon oxides, nitrogen oxides and/or sulfur oxides.    Housing (1)    Magnesium catalyst (13)    Catalyst chamber (14)    Homogenization deflector (16)    Quartz layer (18)
NOVELTY - Producing biofuel or biofuel components, comprises: feeding biological material into a reactor system (5) comprising a catalytically active guard bed phase and main reaction phase, where the feed material (1) is contacted in at least one phases with a combination of hydrodeoxygenating (HDO) and hydrodewaxing (HDW) catalysts; treating the feed material catalytically with hydrogen in the system to cause hydrodeoxygenation, isomerization and cracking of feed material components to provide a hydroprocessing product; and recovering at least a fraction of the product as biofuel.    USE - The method is useful for producing biofuel or biofuel components (claimed).    ADVANTAGE - The method allows economical and efficient production of biofuel or biofuel components with high yield, quality and acceptable ignition and cold flow properties.    DETAILED DESCRIPTION - INDEPENDENT claims are included for:    (1) use of a hydrocarbon fraction produced by the method as a fuel or an additive in fuel compositions; and    (2) fuel having characteristics meeting specification EN 590 diesel and comprising at least one hydrocarbon fraction produced by the method.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a process for producing biofuel or biofuel components.    Feed material (1)    Feed tank (2)    Reactor system (5)    Separator (6)    Hydrogen source. (7)
NOVELTY - Processing lignocellulosic substrate comprises: (a) providing a lignocellulosic substrate; (b) contacting the lignocellulosic substrate with an extractant comprising a water-soluble organic solvent to form an extracted substrate and a miscella; (c) removing miscella from the extracted substrate; and (d) hydrolyzing the extracted substrate using a chemically catalyzed process.    USE - The method is useful for processing lignocellulosic substrate (claimed) including wood, which is useful for forming conversion product including methane, ethanol, butanol, isobutanol, a fatty acid, a fatty acid ester, a fatty alcohol and biodiesel.    ADVANTAGE - The method: provides a faster filtration rate by at least 10% compared with a filtration rate of lignin solids from hydrolyzate formed by hydrolyzing without the extracting, using an identical filter and identical filtration conditions (claimed); recovers the solvent and/or the weak acid from the miscella, which contributes to a reduction in process costs; and doest not provide impurities in the lignin present in hydrolyzate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a system comprising: an extraction module adapted to extract the lignocellulosic substrate with an extractant comprising a water soluble organic solvent and a weak acid, and to output an extracted substrate and a miscella; and a hydrolysis module adapted to receive the extracted substrate and to contact it with hydrochloric acid at a concentration of at least 30% to produce an acid hydrolyzate; and    (2) a lignocellulosic composition, comprising (on a dry matter basis) cellulose, hemicellulose and lignin, and characterized by at least two of less than 5000 ppm lipophilic material, less than 5000 ppm ash, less than 2000 ppm calcium, less than 10000 ppm pectin, less than 2000 ppm furfural, at least 10 ppm marker (comprising furfural, organically bound sulfur or a water soluble solvent) or a moisture content of 5-30%.
NOVELTY - Nerium biodiesel has a kinematic viscosity of 3.6 cst at 40 degrees C, a cetane number of 45, a calorific value of 42923 kJ/kg, a density of 850 kg/mm3 at 15 degrees C, a flash point of 70 degrees C, and a fire point of 83 degrees C.    USE - Nerium biodiesel is used in diesel engines.    ADVANTAGE - Nerium biodiesel is environmentally-friendly and has excellent performance characteristics nearing diesel. Emission of hydrocarbon and carbon monoxide is reduced. The biodiesel can be used in existing diesel engines without compromising the engine performance. Nerium oil, being non-edible oil proves to be a very effective alternate fuel. After transesterification of Nerium oil, kinematic viscosity and density are reduced while the calorific value is increased.
NOVELTY - The method involves subjecting the cashew nut shell oil to distillation and filtrations process to remove the solid and floating impurities. The cashew nut shell oil is passed through activated charcoal. The cashew nut shell oil is hydrogenated to hydrogenation process. The hydrogenated oil is subjected to cracking process. The cracked oil is mixed with ethanol in a predetermined proportion, such that blended oil is served to use as bio-fuel.    USE - Method for preparing green petrol from cashew nut shell oil.    ADVANTAGE - The highly volatile cracked oil is mixed in a proportion by volume with ethanol, so that blended oil can be served as a fuel in an internal combustion engine. The biofuel is used to carry a series of engine tests on an internal combustion engine such as four stroke petrol engine, so that efficiency of the biofuel can be checked efficiently. The distillation and filtration of the oil are passed through active charcoal to reduce the calcium sodium and sulphur ions which are subjected to hydrogenation and cracking. The cracking increases the yield of green petrol, so quality of gasoline can be improved.
NOVELTY - The machine has a U shaped charcoal chamber (1) with extension area (13) that is made of stainless steel. A rotating centre pipe (3) is fixed with rotating flights (2) to transfer the coconut shells from the feeding point to the discharge point. MS shaft (4) is attached to the both sides of the centre pipe and is coupled with the front end and rear end bearings with the block (5,16).    USE - Mechanical machine for making charcoal from coconut shell.    ADVANTAGE - The charcoal can be produced continuously throughout the year efficiently. The machine can be operated by less labor force. The skilled work force needed to operate machine can be avoided. The carbon monoxide present in the emitting flue gas can be avoided. The quality of charcoal can be improved. Maximum amount of heat in the flue gas can be recovered as hot air through the hot air recovery portion of the machine. Charcoal from the machine can be directly converted to activated carbon by simply connecting the activation chamber to machine, thus the production cost of activated carbon can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a front isometric view of the charcoal machine.    U shaped charcoal chamber (1)    Rotating flights (2)    Rotating centre pipe (3)    MS shaft (4)    Front end bearing with block (5)    Charcoal chamber extension area (13)    Rear end bearing with block (16)
NOVELTY - Manufacturing of biodiesel from vegetable oil in the presence of acid catalyst involves esterification reaction, product purification and methanol separation, purification and re-cycling.    USE - For manufacturing biodiesel from vegetable oil (claimed), which is used as substitute for petro-diesel fuel.    ADVANTAGE - The process is an optimized process. The process is more efficiently and economically carrying out the acid catalyzed esterification on fatty acid of vegetable oil. The esterification is carried out in a bubble column reactor that provides a highly efficient reaction at relatively high temperatures.
NOVELTY - The system (300) has a distribution board (325) that is connected to a fuel cell unit (315) and to cooling energy management units (CEMU) (335a-335n) such that, in case of power failure, the fuel cell unit provides the required energy to the system. The fuel cell provides constant energy to the board which transfers the energy to the CEMUs and a base transceiver station (330). The CEMUs selectively operate one or more heat management units based on the inside temperature, surrounding temperature, and available power at a back-up power source to keep the inside temperature at preset range.    USE - Load surge managing system for building.    ADVANTAGE - Enables provision of a load surge managing system having an energy saving feature that gets activated whenever the ambient temperature is reduced from a preset value, thus avoiding conventional air conditioning load which in turn reduces fuel consumption in the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for managing a load surge during and after transition of power from a primary power source to a back-up power source.    DESCRIPTION OF DRAWING(S) - The drawing shows the high-level block diagram of the load surge managing system.    Load surge managing system (300)    Fuel cell unit (315)    Distribution board (325)    Base transceiver station (330)    CEMUs (335a-335n)
NOVELTY - An odorization agent-removal apparatus consists of container containing adsorption agent comprising Y-type zeolite of silver support.    USE - Odorization agent-removal apparatus used for removing odorization agent e.g. mercaptan, sulfide and cyclohexane in raw fuel for fuel cell e.g. polymer electrolyte fuel cell and solid oxide fuel cell (all claimed) for steam reforming device.    ADVANTAGE - The odorization agent-removal apparatus effectively removes mercaptan, sulfide, cyclohexane and thiophenes and prevents carbon deposition on surface of modification catalyst of modification portion of steam reforming device and increases hydrogen production efficiency.
NOVELTY - The generator has a reaction chamber with a first electrode (19) and a second electrode connected to poles. The second electrode secured to a base (13) includes concentric walls (14) whose height is greater than length of the first electrode. Covers (15) and the first electrode are attached to a top plate (18) of the reaction chamber. Symmetry axes of the first electrode are spaced apart on a set of coaxial lines between the concentric walls. An accumulation chamber (3) is located above an upper plate of the reaction chamber, and separated from another accumulation chamber (6).    USE - Hydrogen and oxygen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a hydrogen and oxygen generator.    Accumulation chambers (3, 6)    Base (13)    Concentric walls (14)    Covers (15)    Top plate (18)    Electrode (19)
NOVELTY - A magnesium-ammonium phosphate production suppression system has methane fermentation tank (7), ammonia-removal equipment which removes ammonia in the methane fermentation digestive liquid from the methane fermentation tank, and carbon dioxide gas-dissolving apparatus (200) which dissolves carbon dioxide gas in the methane fermentation digestive liquid from the ammonia-removal equipment.    USE - Magnesium-ammonium phosphate production suppression system is used for methane fermentation system (claimed) for processing livestock dung discharged from hoggery and poultry farm, wastewater treatment of sewage sludge, and foodstuff waste material.    ADVANTAGE - The methane fermentation process is efficiently performed by the methane fermentation system provided with the magnesium-ammonium phosphate production suppression system, with suppressed precipitation of magnesium-ammonium phosphate scaling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane fermentation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane fermentation system. (Drawing includes non-English language text)    Ammonia fermenter (2)    Methane fermentation tank (7)    Heater (8)    Heat exchanger (9)    Carbon dioxide gas-dissolving apparatus (200)
NOVELTY - A hydrogen generating apparatus (100) comprises modifier (4) which generates hydrogen-containing-gas by reforming reaction using a raw material and is arranged to transfer heat, hydrodesulfurization device (3) which removes sulfur compound in raw material supplied to modifier, and heat-transfer buffer part (5) which is arranged between modifier and hydrodesulfurization device and buffers the heat transfer from modifier to hydrodesulfurization device in which flow of raw material in modifier is from upstream part to downstream part.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Desulfurization performance is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional schematic view of the hydrogen generating apparatus. (Drawing includes non-English language text).    Hydrodesulfurization device (3)    Modifier (4)    Heat-transfer buffer part (5)    Hydrogen generating apparatus (100)
NOVELTY - The apparatus has a desulfurizer which removes the sulfur compound from the raw material added with the hydrogen gas to obtain the desulfurization raw material. A hydrogen generator (6) generates the fuel gas having hydrogen as a main component from the desulfurization raw material for generating fuel cell electric power. A steam separator operates hydrogen generator and hydrogen gas supply source (2) to reduce the water steam in hydrogen gas through water steam separation membrane for performing hydrodesulfurization process.    USE - Hydrogen generating apparatus for use with fuel cell power generating device.    ADVANTAGE - The steam separator operates hydrogen generator and hydrogen gas supply source to reduce the water steam in hydrogen gas through water steam separation membrane for performing hydrodesulfurization process, hence the water vapor contained in the recycle gas can be separated and removed efficiently. The simplified structure can be achieved. The condensed water can be solved, even if the raw material with a high concentration of the sulfur compound. The hydrodesulfurization process can be performed stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Hydrogen gas supply source (2)    Hydrodesulfurization device (5)    Hydrogen generator (6)    Combustion fan (11)
NOVELTY - A metal complex contains dicarboxylic acid compound and metal ion e.g. magnesium, calcium, aluminum, chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc, and/or cadmium as organic ligand in which bidentate coordination is possible. The complex has a two-dimensional sheet structure which carries out mutual penetration.    USE - A metal complex for adsorbent or occlusion material of hydrogen molecule, carbon monoxide, carbon dioxide, oxygen molecule, nitrogen molecule, 1-4 carbon-containing hydrocarbon, noble gas, hydrogen sulfide, ammonia, sulfur oxide, nitrogen oxide, siloxane, water vapor, or organic vapor (all claimed).    ADVANTAGE - Metal complex has excellent adsorption performance of various gases.    DETAILED DESCRIPTION - A metal complex of formula M1A1D1 contains dicarboxylic acid compound of formula (I) and metal ion e.g. magnesium, calcium, aluminum, chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, copper, zinc, and/or cadmium as organic ligand in which bidentate coordination is possible. The complex has a two-dimensional sheet structure which carries out mutual penetration.    R1-R4=H, optionally substituted 1-4C alkyl, 2-4C alkenyl, 1-4C alkoxy, NO2, CN, COOH, sulfone, OH, 1-4C monoalkylamino, 2-8C dialkylamino, 2-4C acylamino, or halo;    M=metal ion;    A=di-anion of dicarboxylic acid compound; and    D=organic ligand in which bidentate coordination is possible.
NOVELTY - This utility model claims a kind of waste oil in the kitchen waste processing device of deep de-sulfurization agent of fuel oil, comprising an oil-water separator (2), esterification reactor (3) and sedimentation separator (6), an oil-water separator (2) through the oil delivery pipeline (9) is connected with the inside of the esterification reactor (3) is provided with a catalyst inlet (4) is set on the esterification reactor (3), reactor (3) by a liquid transmission pipe (11) is connected with the inside of the sedimentation separator (6) is provided with an exhaust port on the sedimentation separator (6) (5), a slag-drip opening (7) and a fuel oil outlet (8). This utility model through the matching use of oil-water separator, the esterification reactor and depositing separator, is featured with simple production process, the production equipment is a totally enclosed, it will not cause secondary pollution to the environment, and so as to realize the energy shortage, the resource recycling, kitchen garbage for preventing liquid in the waste oil returns table and promotes the development of the biological fuel oil sufficiently.
NOVELTY - The reactor has a rectangular-shaped reaction chamber (1) whose upper portion is provided with a rectangular top cover. The water jacket (2) is provided in the chamber. The center of the top cover is provided with a sampling pipe (4) and rotary valve (5). The sampler is fixed with chamber through a sampling pipe. The UV lamp tube is arranged in lower portion of sampler. A display is arranged on top portion of sampler. A temperature sensor is arranged at lower end of rubber gasket. A motor (10) is connected with spiral stirring paddle (8) arranged on the bottom of chamber.    USE - High-efficient anaerobic compost reactor.    ADVANTAGE - The anaerobic compost can be processed easily and effectively. The stack temperature can be measured accurately by the temperature sensor device. The water jacket is provided in the outer reactor wall, to ensure the constant temperature effect of reactor. The efficiency of the reactor can be improved. The compost sampling process can be performed easily. The technical support for performing research about compost can be provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the compost reactor.    Reaction chamber (1)    Water jacket (2)    Sampling pipe (4)    Rotary valve (5)    Paddle (8)    Motor (10)
NOVELTY - Method for reducing acid value of biodiesel crude product having acid value of 0.8-20 mg potassium hydroxide/g involves dehydrating biodiesel crude product, such that moisture content of the biodiesel crude product is less than 1 wt%, and contacting the dehydrated biodiesel crude product with monohydric alcohol for reaction.    USE - Method for reducing acid value of biodiesel crude product used for preparation of biodiesel oil (claimed).    ADVANTAGE - The method enables reduction of acid value of biodiesel crude product under gentle reaction conditions to achieve stable deacidifying effect, and production of biodiesel oil with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel oil, which involves reducing biodiesel crude product having acid value of 0.8-20 mg potassium hydroxide/g isolating a biological diesel oil, and separating unreacted monohydric alcohol and generated water, to obtain deacidified biodiesel product with a qualified acid value.
NOVELTY - Eliminating or reducing siloxane and color materials in biogas by pre-treatment method, comprises making sludge enter into a concentration adjusting tank; adjusting the concentration of the sludge; dividing the adjusted sludge into two portions, where one portion of the sludge directly enters into an anaerobic digestion tank and the other portion of the sludge is pre-treated and then entered into the anaerobic digestion tank for anaerobic digestion reaction; making the produced biogas enter into a biogas storage tank, desilicating the biogas, and removing the siloxane in the biogas.    USE - The method is useful for eliminating or reducing siloxane and color materials in biogas by pre-treatment method (claimed).    ADVANTAGE - The method protects the biogas utilization device, and reduces the biogas purification treatment cost and the maintenance cost of the biogas utilization device; realizes the intelligent analysis and control, and expands the technical advantage and market acceptability of the sludge anaerobic digestion process technology.    DETAILED DESCRIPTION - Eliminating or reducing siloxane and color materials in biogas by pre-treatment method, comprises making sludge enter into a concentration adjusting tank; adjusting the concentration of the sludge; dividing the adjusted sludge into two portions, where one portion of the sludge directly enters into an anaerobic digestion tank and the other portion of the sludge is pre-treated firstly and then entered into the anaerobic digestion tank to perform anaerobic digestion reaction in the anaerobic digestion tank; making the produced biogas enter into a biogas storage tank, desilicating the biogas, and finally removing the siloxane in the biogas and making the biogas enter into a biogas utilization device.
NOVELTY - An alcoholic composition fuel is obtained by reacting derivative of lower alcohols and/or higher alcohols with light hydrocarbon base oil using additive. The lower alcohol and/or higher alcohol are methanol and/or isopropyl alcohol. The additive contains acetal, metal corrosion inhibitor, acetone and methyl tertiary butyl ether.    USE - Alcoholic composition fuel is used for vehicle.    ADVANTAGE - The alcoholic composition fuel has excellent workability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcoholic composition fuel.
NOVELTY - Synthesizing hydrogen fuel involves: uniformly mixing hydroboron, hydroxide, water-absorbent material and catalyst to obtain hydrogen storage material, where the weight ratio of the hydroboron, hydroxide, water-absorbing material, and catalyst is 100:0.01-50:0.1-25:0.01-50; adding water, hydroborate and hydroxide into the hydrogen storage material to form alkaline solution, where the water-absorbing material absorbs alkaline solution to form gel hydrogen storage material; and hydrolyzing the hydroboron in presence of catalyst, to obtain hydrogen fuel.    USE - For synthesizing hydrogen fuel (claimed).    ADVANTAGE - The method can control releasing speed of hydrogen, and provides hydrogen fuel with high purity.
NOVELTY - The device has discharge hole that is formed with the separator (32). A rectifying tank (33) of the separator is connected with the biological diesel oil outlet. A return tank (34) is connected with the reactor (31) and the discharge hole is formed with the material source.    USE - Device for preparing biological diesel oil.    ADVANTAGE - The occurrence of waste in the reactant can be prevented. The production cost of the diesel oil preparation device can be reduced with high product yield and purity.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the device for preparing biological diesel oil.    Reactor (31)    Separator (32)    Rectifying tank (33)    Return tank (34)    Alcohol-oil mixer (35)
NOVELTY - Ore catalytic bed biomass fast pyrolysis oil-making device comprises a feeding system, a hot carrier gas system, an ore catalytic bed pyrolysis reactor, a gas-solid separation and carbon collecting system, a fractional condensing system and a pyrolysis tail gas processing system.    USE - Used as an ore catalytic bed biomass fast pyrolysis oil-making device.    ADVANTAGE - The device: has fast pyrolysis speed; ensures complete pyrolysis, and produces high quality biomass oil with good yield; and is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the ore catalytic bed biomass fast pyrolysis oil-making device.
NOVELTY - The system has a feeding unit (1), pyrolytic reaction unit (2), a discharging unit (3) and a pyrolytic reaction control system (4) which are connected to each other. The pyrolytic reaction unit is provided with a spiral pushing device (22) arranged between pyrolytic reaction element (21) and air supplying device (23). The pyrolytic reaction unit is a rectangular cavity provided with a metal casing. The pyrolytic reaction unit cavity is vertically divided into two portions.    USE - Biomass gas and biomass charcoal preparation system.    ADVANTAGE - Due to the arrangement of heat insulation layer in the pyrolytic reaction unit, the metal casing and a high-temperature reaction medium are effectively separated, and requirements for heat resistance of material of the pyrolytic reaction unit cavity can be reduced. Ordinary steel material can be adopted to reduce cost and effectively relieve temperature distortion of the metal casing. Thus, the heat loss of the system can be reduced. Since the pyrolytic reaction unit is vertically divided into two portions, a bottom quick-wear portion of the reaction unit can be dismantled easily. The maintenance and replacement properties of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gas and biomass charcoal preparation system.    Feeding unit (1)    Pyrolytic reaction unit (2)    Discharging unit (3)    Pyrolytic reaction control system (4)    Pyrolytic reaction element (21)    Spiral pushing device (22)    Air supplying device (23)
NOVELTY - A cleaning agent is obtained by mixing 50 wt.% methanol, 40 wt.% ethanol, 5 wt.% toluene and 5 wt.% cyclohexane, and stirring at normal temperature.    USE - Cleaning agent is used for ternary catalytic converter.    ADVANTAGE - The surface of ternary catalytic converter is efficiently cleaned using the cleaning agent. The ternary catalytic converter cleaned using the cleaning agent has excellent durability, increased automobile power with reduced oil consumption.
NOVELTY - A cleaning agent is obtained by mixing 60 wt.% methanol, 25 wt.% ethanol, 7 wt.% toluene and 8 wt.% cyclohexane, and stirring at normal temperature.    USE - Cleaning agent is used for ternary catalytic converter.    ADVANTAGE - The surface of ternary catalytic converter is efficiently cleaned using the cleaning agent. The ternary catalytic converter cleaned using the cleaning agent has excellent durability, increased automobile power with reduced oil consumption.
NOVELTY - This utility model claims an integrated biological desulfurization device is provided with at least two layers of packing area in the desulfurization reactor, each layer of the packing region at a certain distance. This utility model is a certain distance in the desulphurization reactor layered filler area, the methane and the contact area of the filler is greatly increased, a filler and a reloading is more convenient and fast. The utility model is provided with a single air inlet of the biogas separating, but also directly into the air in the liquid storage layer and the bottom of the reactor, the methane and air will not contact, which greatly increases the safety of the biological desulphurization reaction, and trumpet guide tube the circulating liquid can be smoothly downwards in a filler area, the utility model changes the original single spraying pipe, the spraying pipe is set on each of the trumpet guide tube outer side, the nutrition solution spraying is more balanced.
NOVELTY - The device has air flow channels that are communicated with air gathering pipe (33) and fermentation tanks through opening and closing of valves (41-46) and are passed through fan (32). The fan is positioned to blow air in gathering pipe to fermentation tank with positive-temperature oxygen supply when temperature of stack (55) in fermentation tank is lower than or equal to preset temperature. The fan is positioned to suck air from fermentation tank with negative-pressure oxygen supply when temperature of stack in fermentation tank is higher than preset temperature.    USE - Positive-negative-pressure air distribution device used in compost.    ADVANTAGE - The positive-negative-pressure air distribution device can be switched in the positive-pressure air distribution state or the negative-pressure air distribution state.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the positive-negative-pressure air distribution method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the positive-negative-pressure air distribution device.    Fan (32)    Air gathering pipe (33)    Pipe fittings (34-38)    Valves (41-46)    Stack (55)
NOVELTY - This utility model is a kind of biomass fuel gas system of calcined magnesium oxide, belonging to the biomass gasification heat utilization technology field, wherein a feeding port is installed on the side wall of the gasification furnace, a cyclone dust collector through the gas pipe with the burner, an air pipe through the air nozzle and the rotary kiln, natural gas pipe is installed on the burner and connected with the rotary kiln, fuel gas pipe through the gas nozzle and the rotary kiln, the utility model is of calcined magnesium oxide system, it has high efficiency, stable operation, no pollution, solving the biomass heat utilization technology is difficult to use in the technical problem of calcined magnesium oxide system.
NOVELTY - Preparing plerixafor comprises (a) protecting cyclam with tert butoxycarbonyl (Boc) anhydride to provide 4,8,11-tris-(1-tert-butoxy-vinyl)-1,4,8,11-tetraaza-cyclotetradecane-1-carboxylic acid tert-butyl ester (II), (b) reacting (II) with dihalo-p-xylene to provide tert-butyl 4-((4-((4-tert-butoxycarbonyl-8,11-bis(1-tert-butoxyvinyl)-1,4,8,11-tetrazacyclotetradec-1-yl)methyl)phenyl)methyl)-8,11-bis(1-tert-butoxyvinyl)-1,4,8,11-tetrazacyclotetradecane-1-carboxylate (III), (c) deprotecting in-situ of (III) to provide plerixafor, and (d) purifying.    USE - The plerixafor is useful for treating non-hodgkin's lymphoma and multiple myeloma. No biological data given.    ADVANTAGE - The method prepares the plerixafor in an environmentally-friendly, cost-effective and large scale manner.    DETAILED DESCRIPTION - Preparing highly pure plerixafor comprises: either (a) protecting cyclam with tert butoxycarbonyl (Boc) anhydride to provide 4,8,11-tris-(1-tert-butoxy-vinyl)-1,4,8,11tetraaza-cyclotetradecane-1-carboxylic acid tert-butyl ester (II), (b) reacting (II) with dihalo-p-xylene to provide tert-butyl 4-((4-((4-tert-butoxycarbonyl-8,11-bis(1-tert-butoxyvinyl)-1,4,8,11-tetrazacyclotetradec-1-yl)methyl)phenyl)methyl)-8,11-bis(1-tert-butoxyvinyl)-1,4,8,11-tetrazacyclotetradecane-1-carboxylate (III), (c) deprotecting in-situ of (III) to provide plerixafor of (I), and (d) purifying to provide pure plerixafor; or comprising the step (a) as above per se, (b1) purifying (II) by treating with aqueous acetic acid or silica gel, (c) reacting (II) with dibromo-p-xylene in acetonitrile in the presence of base to provide (III), (d) deprotecting in-situ of (III) with hydrochloric acid to (I), and (e) purifying the plerixafor in a solvent. An INDEPENDENT CLAIM is included for purifying the plerixafor comprising dissolving the plerixafor in the mixture of isopropanol and ethyl acetate to provide a solution, cooling the solution, and isolating the pure plerixafor.
NOVELTY - A micro-emulsified methanol diesel oil comprises 40-90 wt.% diesel oil, 1-40 wt.% methanol, 3-40 wt.% naphthenic acid, 0.1-5 wt.% amine compound, and 0.1-4 wt.% additive. The methanol diesel oil is prepared by mixing diesel oil, methanol, oxidant, and naphthenic acid, adding amine compound, and stirring till transparent solution is obtained.    USE - Micro-emulsified methanol diesel oil is useful as clean fuel for internal combustion engines, industrial kilns, and boilers.    ADVANTAGE - The micro-emulsified methanol diesel oil is economical.
NOVELTY - This utility model claims a fixing coal pressurizing gasification ammonia synthesis gas and liquefied natural gas generation device, comprising a high pressure nitrogen cooler, the first raw material gas cooler, a raw material gas cooler, a nitrogen machine, a nitrogen machine, the nitrogen washing tower, a flash tank, a flash tank, methane rectifying tower, and they are connected by pipeline. The utility model is at the same time preparing ammonia synthesis gas purification, the liquefied natural gas, so as to achieve a low energy-consumption, high investment benefit of high heat value.
NOVELTY - A kind of hydrogen-rich fuel gas generator, it can make the coal or water content of the biomass fuel., domestic garbage and industrial and agricultural organic waste into a hydrogen-rich gas. The character is: fuel gas generator is composed of upper, middle and lower furnace body, high temperature fuel gas outlet of the furnace body and the side of the heat exchanger is connected with the air inlet, wherein the carbon-hydrogen energy conversion is as follows: in the hearth of the furnace body, the oxygen and the steam flows, and top to bottom order a drying and dehydrating section, the oxygen-enriched combustion area, oxygen-poor combustion area and the oxygen-poor combustion region, the lower of the furnace body in the furnace oxygen and water vapour from the upper to the lower, and to form a oxygen-enriched from the upper to the lower in burning area, the lower oxygen-poor combustion zone and a lower anoxic combustion area of carbon or organic substance with oxygen and water vapour in the high temperature environment, along with a continuous change to generate a new material, mainly generating hydrogen-rich gas of carbon monoxide and hydrogen, the hydrogen-rich gas is heat exchanger through the gas flow pipe, is sent to the user through the low temperature fuel gas outlet.
NOVELTY - Microbial agent comprises 20-40% white rot fungus, 5-15% green Penicillium, 10-20% Pseudomonas putida, 5-15% Alcaligenes faecalis, 10-20% Bacillus subtilis and 10-20% Bacillus thuringiensis, accounting to the total bacterial number in the microbial agent.    USE - The microbial agent is useful for effectively degrading organic waste during sewage treatment (claimed).    ADVANTAGE - The microbial agent can rapidly decompose organic waste; effectively inhibits the growth of harmful microorganism, and improves sewage chromaticity and turbidity; facilitates flocculation of suspended particles in sewage; reduces aeration rate, and sludge discharge; and removes bad odor.
NOVELTY - Fir planting composite substrate comprises 200 pts. wt.% fir skin powder, 200-220 pts. wt.% Gendarmerie bran, 0.1-1.2 pts. wt.% corn powder, 10-11 pts. wt.% rice bran, 0.07-0.08 pts. wt.% hydrated lime, 0.04-0.05 pts. wt.% ferment, 0.01-0.02 pts. wt.% cattle liver, 0.01-0.02 pts. wt.% cattle liver, 10-11 pts. wt.% calcium superphosphate, 2-2.5 pts. wt.% calcium-magnesia phosphate fertilizer, 95 pts. wt.% urea and 0.01 pts. wt.% fenaminosulf wettable powder, and is prepared by crushing fir skin yeast adsorption treatment, ectomycorrhizal fungi amplification.    USE - As fir planting composite substrate (claimed), used for growth of fir.    ADVANTAGE - The culture medium for fir skin, makes full use of surplus material of wood processing, it can protect environment and reduce the breeding cost, and quick-acting fertilizer and pesticide, reducing the pollution, avoids soil hardening, saline-alkalized, enhancing the biological activity of the system, improves the soil fertility, fast growth of seedling, good quality and survival rate is high, it has good effect of economic benefit, social benefit and ecological benefit.
NOVELTY - 1 L reeling wastewater is added to bucket, 5-6 g anhydrous citric acid, 13-14 g disodium hydrogen phosphate and 3-4 g tannic acid are added, stirred for 2-5 minutes, heated at 36-37 degrees C, allowed to stand for 50-70 minutes and precipitated. Thus precipitation of sericin in silk reeling wastewater is carried out.    USE - Precipitation of sericin in silk reeling wastewater (claimed).    ADVANTAGE - The method effectively precipitates sericin in silk reeling wastewater with high efficiency in short period of time.
NOVELTY - The biodiesel preparation system has reflux condenser that is connected with reflux condensing pipe (12). A double-layer cylinder (13) is provided with discharge hole (M8) which is set with electromagnetic valve. A separator (6) is connected with buffer tank (7) and static mixer (8). The static mixer is connected to plug flow reactor (9). A grease storage tank (1) and configuration kettle (2) are connected with double-layer glass reaction kettle (5). A data collecting and processing system is provided with pH electrode (15) and sensor (16).    USE - Continuous visualized biodiesel preparation system.    ADVANTAGE - The biodiesel preparation system is provided with simple structure and convenient to operate. The biodiesel can be generated fastly and continuously. The on-line real-time observation of the forming process change of the biodiesel can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous visualized biodiesel preparation system.    Grease storage tank (1)    Configuration kettle (2)    Double-layer glass reaction kettle (5)    Separator (6)    Buffer tank (7)    Static mixer (8)    Plug flow reactor (9)    Reflux condensing pipe (12)    Double-layer cylinder (13)    PH electrode (15)    Sensor (16)    Discharge hole (M8)
NOVELTY - Coaxial variable-speed combined paddle reactor comprises a cylindrical vertical container and a stirring device which is axially installed in the container. The stirring device is a combined paddle of: a ribbon screw stirring paddle which is located in center of the reactor and periphery to a stirring shaft in a top-down position; a lower layer stirring paddle located at the bottom of the reactor; and a bottom stirring paddle located at the bottom of the reactor.    USE - The coaxial variable-speed combined paddle reactor is useful for producing biomass ethanol by simultaneous saccharification and fermentation (claimed).    ADVANTAGE - The reactor enables rapid mixing of the materials and provides even energy distribution; solves the problem of materials sticking close to the wall surface; enhance heat transfer to promote uniform suspension; has simple structure; facilitates convenient adjustment of structural and operating parameters; and convenient to manufacture and install.
NOVELTY - Biodiesel crystallization depressant composition (C1) comprises a triacylglycerol comprising 1,3-dioleoyl-2-palmitoyl glycerol.    USE - The biodiesel crystallization depressant composition is useful in biodiesel fuel.    ADVANTAGE - The biodiesel crystallization depressant composition: exhibits a binary phase behavior; and provides biodiesel fuels with improved low temperature characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biodiesel crystallization depressant composition (C2) comprising a triacylglycerol comprising 2-stearoyl diolein.
NOVELTY - Preparing 2-(1,3-dioxo-1,3-dihydro-isoindol-2-ylmethyl)-1-phenylcyclopropane carboxylic acid diethylamide, comprises reacting 2-(1,3-dioxo-1,3-dihydro-isoindol-2-ylmethyl)-1-phenyl-cyclopropane carboxylic acid with diethylamine in the presence of a coupling reagent, and separating and isolating the 2-(1,3-dioxo-1,3-dihydro-isoindol-2-ylmethyl)-1-phenylcyclopropane carboxylic acid diethylamide.    USE - The process is useful for preparing 2-((1,3-dioxo-1,3-dihydro-isoindol-2-yl)methyl)-1-phenyl-cyclopropane carboxylic acid diethylamide, which is useful as an intermediate for preparing milnacipran (all claimed).    ADVANTAGE - The process provides 2-(1,3-dioxo-1,3-dihydro-isoindol-2-ylmethyl)-1-phenyl-cyclopropane carboxylic acid diethylamide in a cost-effective, environmentally friendly and safe manner.
NOVELTY - Preparing a stable formulation of oxaliplatin having a pH of 4.5-7 comprises dissolving oxaliplatin having purity of at least 98% in water, sparging the solution with carbon dioxide to reduce the pH, and packing the solution in an air tight container for long term storage.    USE - The process is useful for preparing oxaliplatin (claimed), which is useful for treating metastatic carcinoma of the colon or rectum cancer. No biological data given.    ADVANTAGE - The process provides oxaliplatin with high purity of at least 99%, stability and reproducibility in an environmental friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a composition in a unit dosage form comprising an effective amount of oxaliplatin.
NOVELTY - The method involves forming a hydrogen-containing gas from a raw material in a hydrogen generator. Sulfur compounds contained in the raw material is removed in a hydro-desulfurization unit that is heated by heat transfer from the hydrogen generator. Operation of supplying the raw material to the hydrogen generator, is carried out (S103) only when a temperature of the hydro-desulfurization unit is a temperature at which the deposition of carbon from the raw material is suppressed, after the formation of a hydrogen-containing gas in the hydrogen generator is stopped.    USE - Method for operating hydrogen generating apparatus of fuel cell system.    ADVANTAGE - The carbon deposition from the raw material on the hydro-desulfurization catalyst of the hydro-desulfurization device can be suppressed. The possibility that the stable operation of the hydrogen generating apparatus is impaired, can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the operation of the hydrogen generating apparatus. (Drawing includes non-English language text)    Step for determining whether temperature of hydro-desulfurization device is predetermined temperature or less (S101)    Step for carrying out operation of supplying raw material to hydrogen generator only when temperature of hydro-desulfurization unit is temperature at which deposition of carbon from raw material is suppressed, after formation of hydrogen-containing gas in hydrogen generator is stopped (S103)
NOVELTY - Preparing clopidogrel bisulfate comprises preparing alpha bromo(2-chloro) phenyl acetic acid by treating 2-chloro phenyl acetic acid with N-bromo succinimide in the presence of a radical initiator and using dialkyl carbonate as solvent.    USE - The method is useful for preparing clopidogrel bisulfate such as racemization of (R) isomer of clopidogrel, and clopidogrel bisulfate form I (all claimed), where the clopidogrel bisulfate is useful for treating thrombosis. No biological data given.    ADVANTAGE - The method simply and rapidly prepares clopidogrel bisulfate with high yield without using chloroform or carbontetrachloride, thus avoiding anhydrous environment and toxic reagents.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process-I of racemization of (R) isomer of clopidogrel in presence of alkali amides such as sodium amide or potassium amide, or in the presence of organic base comprising tertiary cyclic or acyclic amines such as tertiary butyl amine, triethyl amine, pyridine, pyrolidine or piperidine; and    (2) preparing clopidogrel bisulfate form I comprising dissolving clopidogrel free base in a mixture of ethyl acetate-cyclohexane followed by addition of sulfuric acid.
NOVELTY - The device has a main portion whose upper portion is provided with an odor source (1), a submerged jet aerator (2) and an aeration tank (3). The odor source is provided with a vent hole (4) and a gas conveying pipeline (5). The gas conveying pipeline is provided with a diving jet aerator. The sewage malodorous gas of the odor source is entered into submerged jet aerator. The submerged jet aerator is arranged on the aeration tank by pipeline. The malodorous gas mixed with the sewage is transmitted into the aeration tank.    USE - Municipal sewage integrated deodorization and sewage processing device.    ADVANTAGE - The design, operation and management of the deodorization device can be simplified, and the investment and operation cost can be reduced. The effective processing of malodorous material can be ensured and the good processing effect can be ensured. The convenient operation and good adaptability can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the municipal sewage integrated deodorization and sewage processing device.    Odor source (1)    Submerged jet aerator (2)    Aeration tank (3)    Vent hole (4)    Gas conveying pipeline (5)
NOVELTY - Utilization method of debris and blood drainage liquid in beef processing involves allowing blood drainage liquid to enter into sedimentation tank by filter screen, collecting debris on filter screen and sediments in the settling tank, drying, sterilizing, and crushing the collected sediments to obtain feed protein raw material, where the sedimented liquid is led into a biogas digester for ferment and producing biogas.    USE - The method is useful for utilizing debris and blood drainage liquid in beef processing (claimed) of cattle, sheep, and pork.    ADVANTAGE - The method is environmentally-friendly, cost-effective, simple and convenient to treat, and the value of the debris and blood drainage liquid can be increased by more than 1000 yuan when every 100 cattle are processed.
NOVELTY - The device has a pyrolysis furnace (1) formed with a gas outlet that is matched with a filter (2), a first-stage condenser (3), a second-stage condenser (4), a gas-water separator (8) and a flow meter (10). An air storage tank (11) is formed with a liquid outlet. The liquid outlet is matched with the second-stage condenser and a condenser liquid storage tank (7). The condenser liquid storage tank is connected with the gas-water separator that is formed with a gas liquid separator outlet. The gas liquid separator outlet is matched with a liquid storage tank (9).    USE - Coal, biomass, waste tire and waste organic sludge carbon-containing substance pyrolysis evaluation device.    ADVANTAGE - The device is easy to operate, and effectively realizes carbon-containing substance pyrolysis evaluating process and reduces production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a coal, biomass, waste tire and waste organic sludge carbon-containing substance pyrolysis evaluation device.'(Drawing includes non-English language text)'    Pyrolysis furnace (1)    Filter (2)    First-stage condenser (3)    Second-stage condenser (4)    Condenser liquid storage tank (7)    Gas-water separator (8)    Liquid storage tank (9)    Flow meter (10)    Air storage tank (11)
NOVELTY - Methanol and Xanthium strumarium oil are reacted in molar ratio of 5-12:1 at 55-70 degrees C for 0.5-2 hours, such that amount of potassium hydroxide catalyst is 0.5-1 wt.% with respect to oil. After completing the reaction, petroleum ether is added based on oil/petroleum ether molar ratio of 1-3:1, and maintained for stratification for 10 minutes. Residue is then removed, and solution is washed with water to neutral. Resultant product is subjected to vacuum distillation at 60-90 degrees C under pressure of 0.07-0.08 MPa to obtain Xanthium strumarium oil biodiesel.    USE - Preparation of Xanthium strumarium oil biodiesel (claimed).    ADVANTAGE - The method efficiently and economically provides Xanthium strumarium oil biodiesel without affecting the environment, by simple method.
NOVELTY - An organic-inorganic fertilizer comprises 7-12 pts. wt. potassium chloride, 0-18 pts. wt. calcium superphosphate, 15-20 pts. wt. urea, 0-25 pts. wt. calcium-magnesia phosphate fertilizer, 5-8 pts. wt. white mud, 25-40 pts. wt. grass carbon, 18-35 pts. wt. oil cake, and 0-10 pts. wt. ammonium bicarbonate.    USE - Organic-inorganic fertilizer.    ADVANTAGE - The fertilizer is pollution-free fertilizer.
NOVELTY - Reduction of waste oil viscosity comprises processing waste oil using ultrasonic homogenizing device, separating through inorganic ceramic membrane separator, filtering, and backwashing waste oil.    USE - Method for reducing waste oil viscosity (claimed) used for producing biodiesel raw material.    ADVANTAGE - The method reduces 20-30% viscosity and cost of production device, improves production efficiency, and conserves energy.
NOVELTY - This utility model claims a biomass fuel gas generator, comprising a furnace body and a liner on the inner wall of the furnace body, the furnace body is opened with a feeding port, the lower part in the furnace body is provided with a dust hopper, the bottom bucket chamber and is connected to the upper end, inner container is internally provided with a storage hopper, the upper part of inner container is provided with an air inlet, the air inlet is connected with the air blower, the upper part of the ash bucket is provided with an air outlet, the lower part of liner protruding inwards is formed with wedge. This utility model is convenient to operate, stable combustion, to generate a gas tar amount, high heat value.
NOVELTY - This utility model relates to waste utilization device of wood biological material, a wood material biological comprehensive utilization device, comprising a carbonizing furnace, a furnace door on the furnace side of furnace door is equipped with a handle, side of the carbonizing furnace is further provided with a inert gas inlet, wherein the furnace top is provided with a condensing pipe is connected with the first grade condensing chamber, a condensing chamber and a second level condensing chamber is connected with the second level condensing tube, the condensing chamber and the bottom of the second level condensing chamber is arranged to collect a pipeline. This utility model has simple structure, convenient implementation, furnace heating wire heating, heating is faster, in addition, connected to a condensing chamber and the carbonization furnace, and a condensing chamber, a barrier plate, water, tar and vinegar liquid and gas attached on the block plate, the condensing effect of the effect, the gas tar and vinegar, tail gas also is more environment-friendly.
NOVELTY - A biomass double-stage spiral feeding device, comprising a primary spiral conveying device are connected in turn, a buffer tank and a secondary spiral conveying device, the top wall of the buffer tank is provided with a service port, a buffer tank is provided with the lower part of the ejector is set with a stopper, the stopper of the first level spiral conveying device comprises a closed passage a level spiral conveying device channel port of the swing cover board, middle and a rotary base, wherein the rotary support is fixed on the inner side of the buffer tank top wall, a rotating base is movably connected with middleware, middleware and swing cover plate connected to the periphery of the spiral conveying device is provided with a buffer passage opening, the swing plate is movably installed on the first level spiral conveying device channel port. The utility model prevents the material and gas in the reactor is reverse to the conveying passage of the first level spiral conveying device under the high temperature positive and negative pressure effect, which avoids flying in the air caused by the air pollution.
NOVELTY - This utility model claims a liquefied natural gas joint liquid nitrogen device, a main heat exchanger and the denitrification tower is connected with the liquid phase outlet of the tower, a main heat exchanger and a LNG flash tank are connected with gas phase outlet of the tower and main heat exchanger, nitrogen-methane fractionating tower are connected in turn, a liquid phase outlet of the main heat exchanger a nitrogen-methane fractionating tower and the LNG flash tank are connected in turn, the nitrogen-methane fractionating tower gas phase outlet of the main heat exchanger, the nitrogen compressor, a nitrogen cooler, main heat exchanger and liquid nitrogen storage tank are connected in turn, the gas phase outlet and the liquid nitrogen-nitrogen storage tank for methane fractionating tower gas phase outlet, a liquid nitrogen storage tank of the liquid phase outlet and nitrogen-methane fractionating top tower is connected with the inlet of the main heat exchanger and the composite refrigerant refrigeration system is provided with good environment protection benefit and economic benefit, and the product yield is high.
NOVELTY - This utility model claims a kind of application process in beer factory waste water anaerobic marsh gas combustion system, comprising: means for processing brewery waste water anaerobic marsh gas for dehydrating, dehydrating tank and tank, used for pressurizing the marsh gas compressor for consumption marsh gas burner and marsh gas boiler of the marsh gas, the beer waste water anaerobic processing to marsh gas by marsh gas pipe in turn connected with the dehydration tank, a desulfurizing tank and a compressor, wherein the compressor is connected with a marsh gas burner and marsh gas boiler. This utility model is one kind of can effectively recycle beer waste water anaerobic processing of generating the marsh gas, and it is safe and reliable for use in methane combustion system beer waste water anaerobic processing.
NOVELTY - The method involves drying a wooden piece. Raw materials are separated for removing impurities after the drying process. The raw materials are crushed into a reaction system and split, and a reactor system is cooled at room temperature to obtain biological oil.    USE - Biological oil preparation method.
NOVELTY - Bio-synthesis fuel comprises synthetic fuel comprising 42.97 wt.% methanol, 42.97 wt.% ethanol, 11.73 wt.% castor oil and 1.46 wt.% hydrogen sulfate, and 0.25 wt.% ionic emulsifier, 0.29 wt.% cosolvent, and 0.29 wt.% cresol.    USE - Used as bio-synthesis fuel.    ADVANTAGE - The method uses methanol and ethanol in preparing biological fuel with high calorific value through scientific method; reduces pollution discharge; utilizes easily available and economical raw materials; and is suitable for synthesizing renewable energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biological synthesis method for manufacturing fuel, comprising (i) mixing the raw material according to the weight ratio, adding the selected material into a stirring tank, stirring and mixing uniformly, (ii) placing the uniformly stirred mixed material in a reaction kettle and heating to 350 degrees C, (iii) removing gas of heated mixture through a gas-liquid separator, conveying liquid directly into the catalytic tower, introducing 4 m3/1000 kg hydrogen, then cooling to normal temperature by tube, and (iv) reducing the temperature of the mixed material to the normal temperature and conveying to a finished product tank, and adding 5% ferrocene and 10% octane value to obtain the bio-synthesis fuel.
NOVELTY - Methanol gasoline comprises 35-40 wt.% methanol, 6-8 wt.% blending agent, 0.03-0.07 wt.% functional additive and gasoline (remaining amount). The blending agent comprises 2 pts. wt. acetylacetone, 0.5 pts. wt. fatty acid methyl ester, 1.5 pts. wt. dimethoxymethane, 1 pts. wt. ethanol and 1 pts. wt. alkylborane. The functional additive comprises 0.02 pts. wt. corrosion inhibitor, 0.01 pts. wt. metal deactivator and 0.02 pts. wt. antioxidant T501.    USE - Used as a methanol gasoline.    ADVANTAGE - The methanol gasoline: comprises blending agent which improves miscibility of methanol with gasoline and increases the thermal value and the octane value; comprises functional additive which improves the properties of corrosion resistance, swelling resistance, oxidation resistance and water resistance, and improves the safety of an oil product; is environmentally friendly, and discharge reaches the national five-level standard; and can be stored for more than one year, and can be directly used without changing an engine and a control system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing methanol gasoline, comprising (i) mixing a corrosion inhibitor, a metal deactivator and antioxidant T501 to obtain functional additive; (ii) mixing acetylacetone, fatty acid methyl ester, dimethoxymethane, ethanol and alkylborane to obtain blending agent; and (iii) adding functional additive to methanol, stirring for 30 minutes, then sequentially adding gasoline and blending agent, stirring for 30 minutes, sealing and allowing to stand for 12 hours.
NOVELTY - Improving biodiesel yield by bioenzyme method, involves preparing biodiesel by carrying out enzyme catalytic reaction of short chain alcohol and oil, introducing watering step, removing volatile gas in the enzyme reactor into the low temperature absorbing tank, refluxing gas and dehydrating, gas path continuous circulating into enzyme reactor to improve the reaction conversion rate.    USE - For improving biodiesel yield by bioenzyme method (claimed).    ADVANTAGE - The method effectively promotes the reaction, improves reaction conversion rate and obviously reduces the acid value of the biologic diesel oil product. The short chain alcohol water-absorbing process greatly simplifies the operation steps, and has good economic benefit and environmental benefit.
NOVELTY - Marsh gas treatment system comprises an anaerobic reactor provided with a marsh gas outlet, where the gas outlet and the sealed marsh gas voltage regulation cabinet gas inlet are in sealed connection. The outlet end of the biogas pressure stabilizing cabinet is connected with the air inlet end of the marsh gas combustor and a marsh gas biological desulfurization system. The marsh gas biological desulfurization system comprises: a washing tower, a filler for increasing gas-liquid contact area and a biological washing tower provided with a washing liquid; a bioreactor.    USE - Used as a marsh gas treatment system.    ADVANTAGE - The system subjects the marsh gas to a series of treatment, so that the marsh gas can be well treated and used effectively.    DETAILED DESCRIPTION - Marsh gas treatment system comprises an anaerobic reactor provided with a marsh gas outlet, where the gas outlet and the sealed marsh gas voltage regulation cabinet gas inlet are in sealed connection. The outlet end of the biogas pressure stabilizing cabinet is connected with the air inlet end of the marsh gas combustor and a marsh gas biological desulfurization system. The marsh gas biological desulfurization system comprises: a washing tower, a filler for increasing gas-liquid contact area and a biological washing tower provided with a washing liquid; a bioreactor provided with bioreactor solution, which contains thiobacillus, and an aeration system; and a sulfur precipitator for separating and washing liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas treatment system.
NOVELTY - This utility model claims a high safety performance of the marsh gas purifying gas supply air system, comprising orderly connected with the purifying device, a gas storage device and an air supply device, a purifying device is connected with a constant pressure device, a dehydrating device and device, a gas storage device comprises a pressure relief device and a flexible storage bag which are connected in turn, an air-supply device comprises orderly connected with the pressurizing device, storing device and a pressure regulating valve, and device is connected with a discharging device, a flexible storage bag connected with pressurizing device. Because of gas storage device comprises a flexible storage bag, a pressurizing device used for ensuring the pressurizing device and controlling the start and stop of the stop, for controlling the pressure of the system and improves the safety performance of the system, a pressure regulating valve can be adjusted according to a constant air supply pressure for gas way for air pressure and supplying quantity, safety control device. The marsh gas purifying gas supply system using condition is not limited by season and climate region, not easy to be eroded, a gas storage device good leak tightness, high safety performance and low cost.
NOVELTY - A catalyst contains barium titanate or strontium titanate.    USE - Catalyst is used for manufacturing hydrogen from fuel containing sulfur e.g. natural gas, liquefied petroleum gas, coal reformed gas and low-hydrocarbon gas-containing sulfur compound (all claimed).    ADVANTAGE - The catalyst improves hydrogen generation efficiency, and is economical. The hydrogen is efficiently manufactured using the catalyst without poisoning sulfur concentration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen which involves, reacting fuel containing sulfur with water vapor in the presence of catalyst.
NOVELTY - Maximization of production of ethanol from starchy raw material involves: combining the starchy raw material with microbially spoilt wheat, grinding the mixture into a flour and adding water to it to form a slurry, subjecting the slurry to hydrolysis using liquefying amylase followed by saccharifying amylase, to produce sugar, followed by subjecting the sugar to fermentation using distiller's yeast biomass to obtain ethanol.    USE - For maximizing production of ethanol from starchy raw material (claimed) which is used as a chemical feedstock and for portable purposes is being increasingly used as an automobile fuel.    ADVANTAGE - The method is fast process for fermentation of starchy raw materials to higher concentration of ethanol, using yeast. The method maximize ethanol production in grain based distilleries on a daily basis, by cutting down the fermentation time even in the absence of externally added conventional yeast nutrients; maximizes the production of ethanol without the addition of external yeast nutrients or proteases; maximizes the production of ethanol, without using prolonged periods of fermentation; maximizes the production of ethanol, using normal and rejected versions of raw materials. The method saves the time for subsequent round of fermentation. The method overcomes the problem of prolonged fermentation and that too without the addition of external yeast nutrients or proteases for internal production of organic nitrogeneous nutrients. Besides, it saves sizeable amounts of relatively expensive healthier versions of the raw materials requiring more expensive storage facilities and instead an almost equal weight of rather inexpensive reject is utilized for the purpose. Thus, besides saving the nutrients and the healthier version of relatively expensive starch-containing raw materials, the input such as labor and electricity are also saved, thus leading to reduced cost of production of the final product.
NOVELTY - Preparing mixture of erythro- and threo-2-phenyl-2-(piperidin-2-yl) acetamide comprises treating a 2-phenyl-2-(2-pyridyl)acetamide with palladium on carbon in acetic acid, except any other solvent to provide a 2-phenyl-2-(2-piperidyl)acetamide.    USE - The process is useful for preparing mixture of erythro- and threo-2-phenyl-2-(piperidin-2-yl) acetamide, which is useful as an intermediate for preparing methylphenidate hydrochloride (all claimed) that is useful for treating attention deficit hyperactivity disorder, postural orthostatic tachycardia syndrome and narcolepsy. No biological data given.    ADVANTAGE - The process produces methylphenidate hydrochloride with high yield and purity and improved catalytic activity and efficiency in an environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) one pot synthesis for preparing methylphenidate hydrochloride (I) from threo 2-phenyl-2-(2-piperidyl)acetamide comprising treating 2-phenyl-2-(2-piperidyl)acetamide with methanol, in the presence of a catalyst and an alcoholic hydrochloric acid to provide (I);    (2) a process for preparing (I) comprising treating 2-phenyl-2-(2-pyridyl)acetamide with a reducing agent in the presence of an acid to provide 2-phenyl-2-(2-piperidyl)acetamide, treating the 2-phenyl-2-(2-piperidyl)acetamide with an inorganic base and methanol in the presence of the catalyst and the alcoholic hydrochloric acid to provide (I), and optionally purifying (I) by treating with a solvent; and    (3) purifying (I) in the presence of an alcohol.
NOVELTY - Producing detoxified hemicelluloses hydrolyzate from cellulosic/lignocellulosic materials, comprises: prehydrolysis of the lignocellulosic materials with dilute acid, sulfur dioxide, sodium hydroxide or water at a temperature of 120 degrees C or above, for 30-120 minutes in one stage or in two stages of 30-60 minutes; and detoxification of hemicellulose hydrolyzate by treating with lime and whey.    USE - The process is useful for producing detoxified hemicelluloses hydrolyzate from cellulosic/lignocellulosic materials (claimed).    ADVANTAGE - The process provides detoxified hemicelluloses hydrolyzate with reduced nutrient requirement during fermentation, in a large scale and cost-effective manner.
NOVELTY - Batch process for manufacturing a total moisture free hexa-chloroethane from per-chloroethylene using UV Light from solar energy for micro and small industries, involves: (a) passing chlorine gas into the reactor containing lower chlorinated ethylene; (b) reacting chlorine gas with lower chlorinated ethylene in presence of UV light; (c) chlorination to form hexachloroethane; (d) circulation of cold water through inlet for cooling the exothermic reaction in steel drums; and (e) collection of the final product for crystallization and subsequent filtration by siphoning.    USE - The batch process is useful for manufacturing total moisture free hexa-chloroethane from per-chloroethylene using UV light from solar energy for micro and small industries. The moisture free final product of hexa-chloroethane is useful in aluminum smelters as degassers (all claimed).    ADVANTAGE - The final product is moisture-free, economical and safer to use in aluminum smelter plants as degassers in micro and small industry.    DETAILED DESCRIPTION - Batch process for manufacturing a total moisture free hexa-chloroethane from per-chloroethylene using UV Light from solar energy for micro and small industries, involves: (a) passing chlorine gas into the reactor containing lower chlorinated ethylene; (b) reacting chlorine gas with lower chlorinated ethylene in presence of UV light; (c) chlorination to form hexachloroethane with a temperature not exceeding 60 degrees C; (d) circulation of cold water through inlet for cooling the exothermic reaction in steel drums where the reactors are placed; (e) collection of the final product for crystallization and subsequent filtration by siphoning; and (f) reaction of the tail-end-chlorine (unreacted chlorine) with per-chloro ethylene in closed reactors connected in series to form hexa-chroloethane by batch process.
NOVELTY - The utility model claims a new-type energy-saving integrated sewage treatment device, comprising a water pool, a biochemical pool, and equipment, the cistern and a water inlet pipe is connected with a water pump and an electromagnetic flow meter, the biochemical pool and the cistern is connected with the water inlet pipe, and is provided with an aeration system, is provided with a composite ecological balls on upper part of the aeration system, the device is provided with a fan, a dissolved oxygen detecting instrument and a control cabinet, the air blower and dissolved oxygen detector are respectively connected to the biochemical pool through a pipeline. Automatically adapt water quality and water quantity change when this utility model of sewage treatment device has simple technical process, convenient installation, and automatically passes through variable-frequency control water pump and the rotation speed of the fan, continuous operation, saves a lot of electric energy, and a sludge very little, but the whole self-digestion of the system does not need to set sedimentation tank and sludge pool, convenient management and maintenance, at the same time, avoids the secondary pollution caused by sludge treatment;
NOVELTY - The method involves providing a dryer in which a drying tower (6) with several tower plates (3) is arranged. A hot water pipe (4) is arranged on each tower plate. The tower plate is arranged on the drying tower. The upper portion of the drying tower is provided with a marsh gas outlet (5). The lower portion of the drying tower is provided with a marsh gas inlet (1). The upper portion of the drying tower is positioned with a vapor outlet (2). A tower board drying agent is provided in the drying tower air outlet to perform heat enthalpy.    USE - Method for regenerating biogas dehydration drying agent by utilizing low enthalpy energy.    ADVANTAGE - The marsh gas drying agent and regenerating organic agent are contacted together, hence energy consumption can be reduced. The comprehensive energy can be utilized efficiently. The reproduction speed and drying speed can be improved effectively. The service lifetime of the device can be prolonged. The utilization rate and production efficiency of the source can be ensured. The high enthalpy energy can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas dehydration drying agent regenerating device.    Marsh gas inlet (1)    Vapor outlet (2)    Tower plate (3)    Hot water pipe (4)    Marsh gas outlet (5)    Drying tower (6)
NOVELTY - A biomass heavy petroleum hydrogenating-upgrading catalyst comprises hydrogenating active component, carrier and additive. The hydrogenating active component includes noble metals comprising 1-6 wt.% palladium, 0.5-3 wt.% platinum, 1-4 wt.% rhodium and 0.1-2.5 wt.% ruthenium. The carrier comprises multi-walled carbon nanotube-SBA-15 composition.    USE - Catalyst is used for hydrogenating-upgrading of biomass heavy petroleum component (claimed).    ADVANTAGE - The catalyst having high metal dispersion, large pore diameter and high activating rate is prepared, by simple method. The hydrogenating-upgrading of biomass heavy petroleum component is carried out such that the heat value of heavy petroleum is improved, viscosity of heavy petroleum is reduced, and practicability of heavy petroleum is strengthened, using the catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of biomass heavy petroleum hydrogenating-upgrading catalyst, which involves mixing hydrogenating active component, carrier and additive, filtering, crushing, heating at 500 degrees C for 2-4 hours, adding anionic surfactant and ethanol-acetone aqueous solution and reducing mixture; and    (2) method of hydrogenating-upgrading of biomass heavy petroleum component.
NOVELTY - Preparing temozolomide, comprises: either reacting 5-amino-1H-imidazole-4-carboxylic acid amide (II) with sodium nitrite and hydrochloric acid in water at 0-5 degrees C to obtain 4-carbamoyl-1H-imidazole-5-diazonium (III), cyclizing (III) using methyl isocyanate (MIC) in a solvent to obtain crude temozolomide, and purifying crude temozolomide to obtain temozolomide; or preparing MIC from N-methyl carbamoyl chloride, and reacting the formed MIC with 4-carbamoyl-1H-imidazole-5-diazonium chloride.    USE - The process is useful for preparing temozolomide (claimed), which is useful as an alkylating agent for the treatment of refractory anaplastic astrocytoma, a form of brain tumor, glioblastoma multiforme and metastatic melanoma. No biological data given.    ADVANTAGE - The process provides temozolomide with high yield and purity in an eco-friendly and economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing MIC, comprising reacting N-methyl carbamoyl chloride with pyridine in solvent(s) and at temperature;    (2) a crystalline form X of crude temozolomide having characteristic powder X-ray diffraction pattern having peaks expressed as 2 theta as given in the specification; and    (3) preparing the crystalline form X of crude temozolomide, comprising reacting 4-carbamoyl-1H-imidazole-5-diazonium chloride with methyl isocyanate in dimethyl sulfoxide, and isolating the crystalline form by adding an antisolvent.
NOVELTY - Preparation of 5-chloro-N-(((5S)-2-oxo-3-(4-(3-oxo-4-morpholinyl) phenyl)-1,3-oxazolidin-5-yl) methyl)-2-thiophene-carboxamide (rivaroxaban), comprises: reacting 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one with 5-chloro-thiophene-2-carboxylic acid in the presence of boric acid and/or optionally substituted phenyl boronic acid.    USE - The rivaroxaban is for preventing venous thromboembolism in adult patients undergoing elective hip or knee replacement surgery, and reducing stroke risk in cardiac patients. No biological data given.    ADVANTAGE - The process is simple, ecofriendly, inexpensive, reproducible and robust, and provides rivaroxaban with high yield and high purity.
NOVELTY - Rapid culture of autotrophic dinitrification granule sludge under low substrate concentration and high ascending velocity condition comprises crushing anaerobic ammonia oxidation sludge, mixing uniformly with activated aerobic sludge, feeding into upflow anaerobic sludge bed reactor; adding ammonium sulfate and sodium nitrite; reacting at 25-28 degrees C, setting first low rise velocity at 1-2 m/hour for 1-3 days, adjusting reflux ratio, adjusting velocity to 4-7 m/hour; and culturing for 50-80 days, adjusting hydraulic retention time from 6-8 hours to 0.2-0.5 hour gradually.    USE - Method for rapid culturing autotrophic dinitrification granule sludge under low substrate concentration and high ascending velocity condition (claimed).
NOVELTY - Organic biofertilizer comprises tobacco organic matter as main raw material.    USE - The organic biofertilizer is useful for cultivating tobacco.    ADVANTAGE - The organic biofertilizer provides nutrition to plant, has excellent synergistic action, improves quality and photosynthetic condition of plant, increases yield and growth of crops, can be absorbed by plants easily, improves plant resistance, and enhances plant root development.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the organic biofertilizer, which involves processing the waste of tobacco stalk, carrying out detoxification process in a liquid fermentation tank, fermenting in the solid fermentation tank, drying the fermentation product in the solid fermentation tank, crushing and preparing the biofertilizer, detecting quality, and packaging the obtained fertilizer.
NOVELTY - Preparation of methyl ketone comprises reacting olefin (I), (II) or (III) as raw materials, air or oxygen as oxidant, palladium acetate as catalyst, benzoquinone, sodium nitrite as cocatalyst acid and amfenac as initiator in reaction solvent to give methyl ketone (IV), (V) or (VI). The reaction solvent is water or organic solvent and water. The acid is hydrochloric acid, sulfuric acid, acetic acid, trifluoroacetic acid or perchloric acid. The organic solvent is ethyl acetate, methylene chloride, acetic acid, chloroform, acetonitrile, methanol, ethanol, 1,4-dioxane or N,N-dimethylformamide.    USE - Method for preparing methyl ketone (claimed).    ADVANTAGE - The method is mild and environment-friendly and has high efficiency and selectivity.    DETAILED DESCRIPTION - Preparation of methyl ketone comprises reacting olefin of formula (I), (II) or (III) as raw materials, air or oxygen as oxidant, palladium acetate as catalyst, benzoquinone, sodium nitrite as cocatalyst acid and amfenac as initiator in reaction solvent to give methyl ketone of formula (IV), (V) or (VI). The reaction solvent is water or organic solvent and water. The acid is hydrochloric acid, sulfuric acid, acetic acid, trifluoroacetic acid or perchloric acid. The organic solvent is ethyl acetate, methylene chloride, acetic acid, chloroform, acetonitrile, methanol, ethanol, 1,4-dioxane, N, N-dimethylformamide or dimethyl sulfoxide.    R1-R5=H, 1-4C alkyl, 1-4C alkoxy, fluoro, chloro, bromo, acetoxy, trifluoromethyl or -CN;    m=1-2; and    n=3-13.
NOVELTY - Preparation of 2,6-bichlorobenzene amine comprises subjecting aniline and chloroacetyl chloride to acylation reaction in toluene solvent; directly adding 2,6-dichlorophenol, sodium carbonate or potassium carbonate, and quaternary ammonium salt phase transfer catalyst, and carrying out etherification; adding strong alkali, heating, refluxing, carrying out rearrangement reaction, and post-treating. The strong base is sodium hydroxide or potassium hydroxide.    USE - Method for preparing 2,6-bichlorobenzene amine (claimed).    ADVANTAGE - The method is low cost and environment-friendly, and has short reaction time and high yield.
NOVELTY - Preparation of mecobalamin involves simultaneously adding sodium borohydride aqueous solution and methanol solution of formaldehyde aqueous solution into aqueous solution of cyanocobalamin and cobalt chloride hexahydrate, stirring, reacting, adjusting pH, filtering, vacuum-concentrating, processing obtained concentrated solution using macroporous absorption resin, washing by water, eluting using acetone-water mixed solution, performing neutral alumina absorption, eluting using acetone-water mixed solution, crystallizing and recrystallizing obtained crude product.    USE - Preparation of mecobalamin (claimed).    ADVANTAGE - The mecobalamin is prepared by simple method, with reduced impact on environmental pollution.    DETAILED DESCRIPTION - Preparation of mecobalamin involves dissolving cyanocobalamin and cobalt chloride hexahydrate in deionized water, stirring, maintaining temperature of reaction liquid (L1) at 10-15 degrees C, dissolving sodium borohydride in deionized water, keeping temperature at 0 degrees C, dissolving formaldehyde aqueous solution in methanol solution, simultaneously adding obtained sodium borohydride aqueous solution and methanol solution of formaldehyde aqueous solution into aqueous solution of cyanocobalamin and cobalt chloride hexahydrate, stirring, reacting, maintaining obtained reaction liquid temperature at 10-15 degrees C, adjusting pH of obtained solution as 6, filtering obtained reaction liquid to obtain filtrate by centrifuging, vacuum-concentrating obtained filtrate to obtain concentrated liquid, processing obtained concentrated solution using macroporous absorption resin, washing by water, eluting using acetone-water mixed solution, performing neutral alumina absorption, eluting using acetone-water mixed solution, crystallizing to obtain crude product, and recrystallizing crude product, to obtain refined mecobalamin.
NOVELTY - A fuel comprises 50-85 wt.% methanol, 3-5 wt.% nano additive, 3-15 wt.% aromatic hydrocarbon and 5-30 wt.% solvent naphtha. The nano additive is mixture of dioctyl ester, alcohol oleate and isophorone. The aromatic hydrocarbon is mixture of methylbenzene and dimethylbenzene.    USE - Fuel (claimed).    ADVANTAGE - The fuel has octane number of 100-115, water-resisting property of 15%, and high combustion property.
NOVELTY - This invention discloses a liquid bio-organic fertilizer, comprising a deep seawater bittern ranging from 10 to 90% (w/w) and a fermented culture of Bacillus subtilis ranging from 10 to 90% (w/w). The liquid bio-organic fertilizer can be used to promote the growth of a plant, in particular Lactuca sativa L. var. longifolia.
NOVELTY - Preparing a nicotinamide powder, comprises (a) providing an aqueous solution of nicotinamide and (b) spray drying the solution.    USE - The method is useful for preparing a nicotinamide powder (claimed), which is useful as a food additive and pharmaceutical for treating weight loss, memory disruption, sleep disorders and skin disease of pellagra. No biological data given.    ADVANTAGE - The method allows rapid and economical preparation of the nicotinamide powder with less labor intensive and energy consumption, high stability and yield, good flowability, workability and direct compressibility and low caking tendency and without waste production in an eco-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT claims are included for:    (1) the nicotinamide powder obtained by the method;    (2) use of a fluidized spray dryer for preparing nicotinamide powder; and    (3) a device for preparing nicotinamide powder, comprising the fluidized spray dryer (1), an additional fluidized bed (30) for further drying nicotinamide powder removed from the fluidized spray dryer, a unit (12) for withdrawing nicotinamide fine dust from the fluidized spray dryer, an accumulation unit (21, 22) for accumulating the nicotinamide fine dust and a unit (23) for reintroducing the accumulated nicotinamide fine dust into the fluidized spray dryer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for preparing a nicotinamide powder.    Fluidized spray dryer (1)    Unit for withdrawing nicotinamide fine dust from the fluidized spray dryer (12)    Unit for accumulating the nicotinamide fine dust (21, 22)    Unit for reintroducing the accumulated nicotinamide fine dust into the fluidized spray dryer (23)    Additional fluidized bed. (30)
NOVELTY - The present invention provides a method for producing gold nanoparticles using hydroxyl peroxide in an aqueous alkaline condition in the presence of a biocompatible protecting agent. The method of the invention does not involve toxic reagents and therefore are environmentally friendly. The gold nanoparticles thus produced can be used in biomedical applications including cancer therapy and drug delivery without purification.
NOVELTY - Digestion purification tower, the digestion anaerobic tower, biogas derived natural energy marsh gas production synthesis library production is filtered by the tower to remove the impurities. If the first time filtering not capable of reaching the requirement, filtering for several times to be standard. So as to prevent the produced marsh gas not filtering to corrosion object using marsh gas . According to protect the natural environment pollution. The tower right hexagonal prism shape, also can be designed into other column body, a platform, and the shape of the other geometrical body are combined with each other as a cone, the tower main purifying tower, separating tower, a sedimentation tank.
NOVELTY - Preparation of long-acting natural mineral organic fertilizer comprises crushing 55 wt.% animal manure, 14 wt.% straw, 10 wt.% bentonite, 8 wt.% zeolite powder and 5 wt.% peat into 200 mesh, and uniformly mixing; adding 8 wt.% additive, uniformly mixing, piling and fermenting at 30 degrees C for 1 week; and granulating, drying, sieving, weighing, and packaging.    USE - Method for preparing long-acting natural mineral organic fertilizer (claimed).    ADVANTAGE - The method is simple and easy; has low cost, long fertilizer effective period, and high utilization ratio; and improves agricultural product quality and yield.
NOVELTY - Metal-organic framework material contains transition metal ion and organic ligand bonded by acting force between coordinate bond or molecule in which 3-dimensional network structure specific surface area is 2000-3000 m2/g and pore volume is 1-2 cm3/g.    USE - Metal-organic framework material for methane adsorption and storage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of metal-organic framework material which involves dissolving copper, zinc, cadmium, cobalt, nickel, or manganese nitrate, acetate salt, chloride salt, carbonate, sulfate, or perchlorate:5,5'-(pyridine-2,5-diyl)-isophthalic acid with mass ratio of 2:1 in water, adding organic solvent to mixture, reacting mixture at 40-120 degrees C to obtain metal-organic framework materials, exchanging greater than or equal to 10 times with acetone, vacuum activating at 0 degrees C for 36 hours, and activating at 100 degrees C for 12 hours.
NOVELTY - Gas containing hydrogen sulfide (H2S), carbon dioxide (CO2), methane (CH4), and hydrogen (H2) gas is processed by performing primary pressure swing adsorption process by adsorbing acidic gas components using solid adsorbent to remove H2S and CO2 as 1st purge gas which is CO2-enriched gas containing H2S with low calorific value and obtain 2nd purge gas containing CH4 and H2 and performing secondary pressure swing adsorption process which gathers CH4 from 2nd purge gas to obtain purified gas which is pure hydrogen.    USE - Processing of gas containing hydrogen sulfide, carbon dioxide, methane, and hydrogen gas for hydrogen preparation from coal gas generated in semi-coke production process.    ADVANTAGE - Desulfurization efficiency is high, equipment corrosion is prevented, reaction has high catalytic performance, reaction gas flow is kept low, and carbon monoxide conversion, oxygen removal rate and sulfur removal rate are high.
NOVELTY - Production of special fertilizer includes mixing dehydrated municipal domestic sludge with plant straw powder, adding earthworm, stacking, conducting earthworm digestion, screening the earthworm to obtain sludge mixture, adjusting the organic matter and nitrogen content of sludge and straw mixture, simultaneously adding fungicide, stacking for the second time, turning the pile once, drying, adding borax, potassium chloride (KCl), and calcium superphosphate, and uniformly mixing to obtain the special fertilizer.    USE - Production of special fertilizer used for corydalis tuber (claimed).    ADVANTAGE - The special fertilizer increases the number of flowers per branch of corydalis tuber, provides bright color for a long time, and has simple, convenient, and easy production, low cost, and no pollution. The method solves the problem of sludge treatment.    DETAILED DESCRIPTION - Production of special fertilizer using municipal domestic sludge comprises dehydrating municipal domestic sludge, mixing the dehydrated sludge with plant straw powder at 4-6:1 ratio, adding earthworm, stacking into strip-shaped rectangle, conducting earthworm digestion for 40 days, screening the earthworm to obtain sludge mixture, measuring the nutrient content of sludge and straw mixture, adjusting the organic matter and nitrogen content of sludge and straw mixture to obtain carbon (C)/nitrogen (N) ratio of 25-30, simultaneously adding 0.15 mass% (based on the total mass of sludge mixture) fungicide, stacking for the second time for 8-10 days, turning the pile once, when secondary stacking is finished, using drying device for drying or naturally drying to obtain mixture having water content of less than 5%, adding 0.25 mass% (based on the total mass of the mixture) borax, adding KCl and calcium superphosphate, adjusting the N:phosphorus (P):K ratio at 5:2:9, and uniformly mixing to obtain the special fertilizer.
NOVELTY - An organic biological fertilizer comprises 25-28 pts. wt. sodium humate, 20-25 pts. wt. calcium potash, 0.5-1.5 pts. wt. Bacillus mucilaginosus strain stalk, 0.5-1.5 pts. wt. Bacillus licheniformis stalk, 24-26 pts. wt. fermented rapeseed meal, and 30-38 pts. wt. citric acid bacteria body.    USE - Organic biological fertilizer used for preventing plant disease and insect pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic biological fertilizer comprising uniformly mixing calcium potash, Bacillus mucilaginosus strain stalk and Bacillus licheniformis stalk, adding sodium humate, fermented rapeseed meal and citric acid bacteria body, and fully and uniformly mixing.
NOVELTY - A biogas heating dryer, comprises a shell body (30), the shell body is driven to turn through a gearbox, inclined blades which are arranged in the shell body enable materials to turn, a discharging hopper (31) is arranged above the right end of the shell body, a high-temperature air inlet (32) is formed in the middle of the right end of the shell body, a waste heat air outlet (34) is formed in the upper portion of the left end of the shell body, the biogas heating dryer further comprises a marsh gas furnace.    USE - Biogas heating dryer (claimed).    ADVANTAGE - The hot wind diffusing device can be arranged in a fermentation tank, thus the household garbage can be rapidly fermented and decomposed by unit of the self weight of garbage, weight storage in the tank and the hot wind diffusing device. Moreover, the hot wind produced by the biogas furnace and the waste heat of the dryer are reutilized, and not only is energy saved, but also pollution of environment is reduced.    DETAILED DESCRIPTION - A biogas heating dryer, comprises a shell body (30), the shell body is driven to turn through a gearbox, inclined blades which are arranged in the shell body enable materials to turn, a discharging hopper (31) is arranged above the right end of the shell body, a high-temperature air inlet (32) is formed in the middle of the right end of the shell body, a waste heat air outlet (34) is formed in the upper portion of the left end of the shell body, the biogas heating dryer further comprises a marsh gas furnace, where the high-temperature wind produced by burning in the marsh gas furnace is leaded into the high-temperature air inlet of the dryer through a hot wind pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas heating dryer.    Biogas heating dryer (1)    Shell body (30)    Discharging hopper (31)    High-temperature air inlet (32)    Waste heat air outlet (34)
NOVELTY - An adsorption catalysis heat carrier comprises active inorganic solid material which is reacted with carbon monoxide, carbon dioxide and/or water.    USE - Adsorption catalysis heat carrier used for catalyst (claimed) for biomass pyrolysis/cracking.    ADVANTAGE - The recycling of adsorption catalysis heat carrier is enabled. The oxygen content of the biomass oil produced after performing pyrolysis/cracking using catalyst containing carrier is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass pyrolysis/cracking catalyst, which comprises adsorption catalysis heat carrier or solid heat carrier.
NOVELTY - A biological fuel oil contains mother liquor and jet coal in which pH value of mixture is neutral, weight ratio mother liquor:jet coal is 1:100, and mother liquor consists of 0.5% cobalt naphthenate, 1.5% calcium naphthenate, 1.25% zinc naphthenate, 0.55% iron acetylacetonate, 1% Sun-A1 biological enzyme, 5% dimethylbenzene, 17.5% isopropanol, and 72.7% jet coal.    USE - A biological fuel oil (claimed).    ADVANTAGE - Biological fuel oil reduces emission of harmful gas, saves fuel oil and energy, improves combustion efficiency, and has no side effect to fuel oil device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological fuel which involves diluting cobalt naphthenate, calcium naphthenate, and zinc naphthenate with isopropanol, diluting iron acetylacetonate with dimethylbenzene, stirring jet coal using magnetic force stirrer, heating to 35 degrees C, adding diluted solutions of cobalt naphthenate, calcium naphthenate, zinc naphthenate, and iron acetylacetonate, continuously stirring, controlling temperature to 40-43 degrees degrees C, stirring for 30 minutes, adding Sun-A1 biological enzyme to jet coal, uniformly stirring, adding water, maintaining temperature at 40-43 degrees C, stirring for 3 hours to obtain mother liquor, mixing uniformly mother liquor and jet coal with weight ratio of 1:100 and introducing oxygen to mixture as mixing starts to obtain semi-finished product, stirring semi-finished product in magnetic environment every 1 hour, stopping stirring for 1 hour, and obtaining finished product with neutral pH value after 48 hours.
NOVELTY - Preparation of carbon molecular sieve comprises mixing phenolic resin fine powder waste material, binder and water, and extrusion molding; carbonizing material strip; and adjusting carbonized material hole with pore-forming agent.    USE - Method for preparing carbon molecular sieve used for separating methane/nitrogen gas mixture (claimed).    ADVANTAGE - The method is environment-friendly, simple and low cost, has wide raw material source, and produces stable product that specifically absorbs nitrogen gas.
NOVELTY - Powdered active carbon-microbial zoogloea culture method is carried out by selecting active microbial sludge as strain, adding nutrient salt and aerating until obtaining mature sludge, adding powdered active carbon into mature sludge and keeping nutrient salt concentration and dissolved oxygen concentration in an aerobic tank to obtain microbial encapsulated active carbon floc, then acclimating microbial strain and monitoring water quality until the water quality is stable.    USE - Method for powdered active carbon-microbial zoogloea culture (claimed).    ADVANTAGE - The method requires small area, has easy operation, and can prolong retention time of powdered activated carbon in a water treatment system to enhance treatment effect. Further, water retention time in the aerobic tank is prolonged such that there is no need to increase the original volume of the aerobic tank.
NOVELTY - A water-soluble fertilizer comprises 1000-1500 pts. wt. pine needles, 700-900 pts. wt. sugar residue, 500-700 pts. wt. lees, 600-1000 pts. wt. wheat straw, 600-900 pts. wt. calcium carbonate, 700-1000 pts. wt. iron, 1100-1300 pts. wt. zinc, 500-700 pts. wt. molybdenum and 3500-4200 pts. wt. water.    USE - Water-soluble fertilizer used for activating soil fertility and promoting crop growth.    ADVANTAGE - The fertilizer has rich resources. It is safe and pollution-free. It improves crop yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of water-soluble fertilizer comprises spreading pine needles and wheat straw on bamboo screen at 3-5 cm thickness, placing in cool ventilated place, naturally drying, crushing to obtain 100 mesh powder mixture, mixing powder with sugar residue, lees, bean straw and wheat straw in cask, adding warm water at 30-45 degrees C, stirring uniformly, naturally fermenting for 5-7 days, adding calcium carbonate, iron, zinc and molybdenum, uniformly stirring, UV and ozone sterilizing, and filling.
NOVELTY - Preparation of 2,4-D choline aqueous solution comprises reacting 2,4-D and trimethylamine in an aqueous environment to obtain 2,4-D trimethylamine salt, reacting, stirring, and sealing in ethylene oxide gas.    USE - Method for the preparation of 2,4-D choline aqueous solution used for preparing 2,4-D choline original drug (claimed).    ADVANTAGE - The method is simple, uses easily obtained raw material, achieves good product quality, has high yield of 96-99%, and has good environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing 2,4-D choline original drug, comprising concentrating 2,4-D choline aqueous solution, cooling and crystallizing, filtering, washing, and drying.
NOVELTY - A high purity doxorubicin is prepared by carrying out macroporous resin chromatography of pure doxorubicin solution, prewashing using low concentration acidic organic solvent aqueous solution, and eluting high concentration acidic organic solvent aqueous solution; removing organic solvent, separating eluted component through preparative column chromatography, eluting mobile phase and the sample, and collecting doxorubicin-containing component; and concentrating and crystallizing.    USE - Method for preparing high purity doxorubicin (claimed).    ADVANTAGE - The method is simple and environment-friendly and has low cost and high yield.
NOVELTY - An industrial cracking furnace value maximization model construction method involves establishing a cracking furnace cracking product yield prediction model in an olefin production device, based on steam cracking experiment data. Industrial cracking furnace target cracking product yield data is acquired. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace such that the total value of cracking products produced by the industrial cracking furnace is maximized.    USE - Method for constructing an industrial cracking furnace value maximization model.    DETAILED DESCRIPTION - An industrial cracking furnace value maximization model construction method involves establishing a cracking furnace cracking product yield prediction model in an olefin production device, based on steam cracking experiment data. Industrial cracking furnace target cracking product yield data is acquired and is adopted to correct and check the established prediction model, such that a calculation result of the prediction model and an actual operation result of the industrial cracking furnace are same. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace such that the total value of cracking products produced by the industrial cracking furnace is maximized.
NOVELTY - An oxygen-enriched biodiesel microemulsion apparatus comprises shell (1), vertical stirrer (2), flat mixing blade (5), disc curved leaf pulp (6) and oxygen-enriched water atomizing nozzle (7). The apparatus further comprises feed port, dosing device, oil feed port, oil pump, air inlet, pressure pump, water pipe, oxygen-rich water reserve tank, ozone generator, gas-water mixer, conduit, water storage tank and discharge port.    USE - Oxygen-enriched biodiesel microemulsion apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of oxygen-enriched biodiesel microemulsion comprising introducing crude biodiesel into microemulsion biodiesel device, mixing system, adding 30-80% of National (III) standard diesel and stirring for 5 minutes; adding 2-3 wt.% hydrophilic agent and stirring for 1-15 minutes; adding 2-4 wt.% butanol and stirring for 15 minutes with vertical agitator, where stirring speed is 100-130 revolutions/minute; adding 1.5-2 wt.% isopentane as ignition temperature regulator; and adding 1-20 wt.% oxygen-rich water, stirring for 15 minutes, adjusting speed to 170-200 revolutions/minute, adding 70-90 wt.% 9-cis-octadecadienoic acid as emulsifier, stirring until clear and transparent, adjusting stirring speed to 280-340 revolutions/minute for 40-60 minutes and standing emulsified oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of oxygen-enriched biodiesel microemulsion apparatus.    Shell (1)    Vertical stirrer (2)    Flat mixing blade (5)    Disc curved leaf pulp (6)    Oxygen-enriched water atomizing nozzle (7)
NOVELTY - Roxatidine acetate hydrochloride is prepared by reacting hydroxybenzaldehyde and piperidine to obtain 3-(1-piperidinylmethyl) phenol; reacting 3-(1-piperidinylmethyl) phenol with N-bromopropyl phthalimide to obtain N-(3-(3-(1-piperidinyl) phenoxy) propyl) phthalimide (I); reacting (I) with hydrazine hydrate to obtain 3-(3-(1-piperidinylmethyl)phenoxy)propylamine (II); reacting (II) with hydroxyacetic acid to obtain N-(3-(3-(1-piperidinylmethyl)phenoxy) propyl)hydroxyacetamide (III); and reacting (III) and acetic anhydride and adding hydrochloric acid to obtain roxatidine acetate hydrochloride.    USE - Method of preparing roxatidine acetate hydrochloride (claimed).    ADVANTAGE - The method has simple and convenient operation, utilizes low-cost raw material, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of roxatidine acetate hydrochloride comprises:    (A) reacting hydroxybenzaldehyde and piperidine in methanol system in presence of potassium borohydride and magnesium chloride at 20-65 degrees C for 4-5 hours to obtain 3-(1-piperidinylmethyl) phenol;    (B) reacting 3-(1-piperidinylmethyl) phenol with N-bromopropyl phthalimide in presence of potassium carbonate in non-protonic solvent (ethyl acetate, acetone, acetonitrile or chloroform) at 25-85 degrees C for 8-20 hours to obtain (I);    (C) adding (I) and hydrazine hydrate, adding ethanol, heating and refluxing at 35-80 degrees C for 2-8 hours to obtain (II);    (D) reacting (II) with hydroxyacetic acid at 90 plus minus 5 degrees C and detecting by HPLC to obtain (III); and    (E) adding (III) with acetic anhydride and reacting at 0-50 degrees C for 5-10 hours, washing reaction product with ethanol and isopropyl ether, then dissolving in ethanol, adding hydrochloric acid and adjusting pH value to 7 to obtain roxatidine acetate hydrochloride.
NOVELTY - Catalytic pyrolysis of biological oil comprises mill grinding dried microalgae to obtain microalgae particle, placing microalgae particle in batch autoclave, adding catalyst, and putting in pressure reducing gas sealing; placing in high-pressure and high-temperature molten salt reactor, reacting, cooling, pouring, extracting with organic solvent, and filtering to remove residue and obtain organic phase; and evaporating in a rotary evaporator to remove solvent from organic phase.    USE - Catalytic pyrolysis method of biological oil (claimed).    ADVANTAGE - The microalgae has photosynthetic efficiency, high oil content, short growth cycle, grease per unit area yield, ease of breeding, as well as the occupation of cultivated land. The biological oil is expected to ease dependence on fossil fuels.    DETAILED DESCRIPTION - Catalytic pyrolysis of biological oil comprises mill grinding dried microalgae to obtain microalgae particle, preferably 100 mesh, placing 2 g microalgae particle in batch autoclave, adding 0.02-1.2 g catalyst, and putting in pressure reducing gas sealing at 2-10 MPa; placing in high-pressure and high-temperature molten salt reactor, reacting at 200-410 degrees C, preferably 310-330 degrees C for 0-240 minutes, preferably 20-40 minutes, cooling, pouring, extracting with organic solvent, and filtering to remove residue and obtain organic phase; and evaporating in rotary evaporator to remove solvent from organic phase.
NOVELTY - Preparation of phosphomolybdic acid catalyst comprises mixing 4-6 pts. wt. molybdophosphoric heteropoly acid having Keggin structure (P2+Mo12O403-), 2-3 pts. wt. phthalic anhydride and 1-2 pts. wt. urea. 20 wt.% Aqueous ammonia is added to the mixture and it is heated to 150-200 degrees C for 3-8 hours to obtain viscous intermediate product. The intermediate product is filtered and 4-6 pts. wt. cobalt chloride is added to the filtered thick liquid and heated at 230-280 degrees C. The product is dried and crushed.    USE - Manufacture of phosphomolybdic acid catalyst used for desulfurizing high-hydrogen sulfide gas, semi-water gas, natural gas, ammonia synthesis raw gas and coke-oven gas, sulfur containing gas and low viscosity gas.    ADVANTAGE - The phosphomolybdic acid catalyst having high catalytic activity, selectivity, high organic and inorganic sulfur removal efficiency, desulfurization efficiency of more than 99%, is manufactured by an environmentally-friendly process without using organic solvent.
NOVELTY - Isomerization reaction of straight-chain paraffin comprises placing straight chain paraffin raw material into reactor, in the presence of hydrogen with isomerization catalyst, reacting to generate branched alkane isomerization reaction conditions. The isomerization catalyst is loaded with hydrogenation/dehydrogenation metal component and solid super-acid. The solid super acid is metal oxide loaded with nitrate (NO3-)-radical. The hydrogenation/dehydrogenation metal component is platinum (Pt), palladium (Pd) and/or nickel (Ni).    USE - Method for isomerization reacting straight-chain paraffin (claimed).    ADVANTAGE - The method has low reaction temperature, high conversion rate, and good selectivity.
NOVELTY - Pretreating lignocellulose comprises taking a choline and amino acid ionic liquid aqueous solution as a pretreatment solvent, mixing lignocellulose and the solvent under the protection of nitrogen, stirring at 50-120 degrees C for 5-24 hours and cooling at room temperature, adding a citrate buffer, adding cellulose and reacting it for 3-12 hours at a speed of 150-250 revolution per minutes and a temperature of 40-60 degrees C to obtain sugar liquid including glucose and xylose. filtering and washing a residue, and drying to obtain the pretreated lignocellulose and finally weighing the lignocelluloses.    USE - The method is useful for pretreating lignocellulose from rice straw, corn straw, corn core, wheat straw and sugarcane bagasse by renewable ionic liquid aqueous solution (all claimed).    ADVANTAGE - The pretreatment process can effectively enhance the efficiency of enzymatic hydrolysis of lignocelluloses so as to improve the yield of fermentable reducing sugar, and economically and energy efficiently pretreating the lignocellulose in an environmental friendly and easy manner.    DETAILED DESCRIPTION - Pretreating lignocellulose by a renewable ionic liquid aqueous solution comprises taking a choline and amino acid ionic liquid aqueous solution as a pretreatment solvent according to a weight ratio of 1:5-1:25, mixing lignocellulose and the pretreatment solvent under the protection of nitrogen, stirring at 50-120 degrees C for 5-24 hours and cooling at room temperature, adding a citrate buffer, adding cellulose and reacting for 3-12 hours at a speed of 150-250 revolution per minutes and a temperature of 40-60 degrees C to obtain sugar liquid mainly including glucose and xylose. filtering and washing a residue, and drying to obtain the pretreated lignocellulose and finally weighing the pretreated lignocelluloses.
NOVELTY - Preparation of cephradine comprises reacting 7-aminodeacetoxycephalosporanic acid with silane protective agent in anhydrous solvent to obtain first solution, dissolving activated dihydrophenylglycine in anhydrous solvent, reducing temperature to - 10 to - 30 degrees C to obtain second solution, mixing first and second solution, and condensing; adding purified water, adjusting pH to 0-0.2 by adding hydrochloric acid to condensate, hydrolyzing at 2-15 degrees C, standing and layering hydrolyzate, and collecting water phase, decoloring water phase, adjusting pH to 4.5-5.0, and crystallizing.    USE - Method for preparing cephradine (claimed).    ADVANTAGE - The method is simple and easy, has mild reaction condition and low cost raw material, and produces less pollution and stable product.
NOVELTY - Recycling a pig ordure slurry comprises: injecting a pig slurry into a pig slurry storage tank and pressurizing the stored pig slurry by adjusting the chamber pressure and separating into a solid sludge and a solution; separating vegetable oils in the solution; and then esterificating the vegetable oils to produce biodiesel.    USE - The method is useful for recycling a pig ordure slurry that is used to generate biodiesel and glycerin (all claimed).    ADVANTAGE - The method is capable of efficiently separating the vegetable oils from the pig slurry.
NOVELTY - Biomass fuel mix comprises synthetic biomass fuel and jet fuel with turpentine oil at volume ratio of 5-90:95-10, with density at 20 degrees C of 0.84 g/cm3, and freezing point of less than 70 degrees C.    USE - Biomass fuel mix.    ADVANTAGE - The fuel mix preparation has better low temperature performance, and is simple and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel mix comprising adding raw material turpentine oil in reactor filled with hydrogenation catalyst, processing continuous or intermittent hydrogenation, with hydrogenation catalyst comprising 5-20 wt.% nickel (Ni)/silicon dioxide (SiO2) loaded or palladium/aluminum oxide, or palladium/carbon, or Raney nickel, and continuous hydrogenation reaction including reaction temperature at 200-350 degrees C, under 2-7 MPa, and volume ratio of hydrogen oil and turpentine of 200-1000:1, and intermittent hydrogenation reaction involving reaction temperature at 120-250 degrees C, under 5 MPa, and volume ratio of hydrogenation catalyst and turpentine at 1-15 wt.% for 2-10 hours, continuously or intermittently hydrogenating, and separating hydrogenation catalyst.
NOVELTY - Preparation of biodiesel from waste oil with pyrrolidone alkaline ionic liquid catalyst comprises reacting pyrrolidone alkaline ionic liquid (I) catalyst and halogenated alkane to synthesize intermediates, reacting intermediate and inorganic base, reacting with waste oil and alkyl alcohol at 60-150 degrees C for 1-5 hours.    USE - Method for preparing biodiesel from waste oil with pyrrolidone alkaline ionic liquid catalyst (claimed).    ADVANTAGE - The method is simple, operates under mild condition, ensures easy separation of product and short reaction time, and realizes high utilization rate of raw material. The catalyst is non-toxic, biologically degradable and has high catalytic activity in small dosage.    DETAILED DESCRIPTION - Preparation of biodiesel from waste oil with pyrrolidone alkaline ionic liquid catalyst comprises reacting pyrrolidone alkaline ionic liquid of formula (I) catalyst and halogenated alkane to synthesize intermediates, reacting intermediate and inorganic base, reacting with waste oil and alkyl alcohol at 60-150 degrees C for 1-5 hours.    n=1-8; and    R=H, 1-12C alkyl, hydroxyethyl or vinyl.
NOVELTY - Alkali catalyzed synthesis of biodiesel comprises mixing oil having free fatty acid content of less than 1.5 mg potassium hydroxide (KOH)/g with 0.5-4% (based on the amount of oil) bentonite having water content of less than 5%, granularity of 100-400 mesh, and montmorillonite content of more than 70%, stirring for 10-60 minutes, adding methanol, which is 5-16 times the mol of oil and 0.2-2% (based on the amount of oil) alkali catalyst, reacting at 50-70 degrees C for 30-120 minutes, standing, separating out the lower layer, and obtaining crude biodiesel.    USE - Alkali catalyzed synthesis of biodiesel (claimed).    ADVANTAGE - Compared with the prior art, the method has increased biodiesel yield by 2-5%, lower requirements on the raw oil and alkali catalyst, reduced dosage of catalyst by 20-50%, less soap produced, and greatly reduced difficulty of subsequent refining.
NOVELTY - Alcohol-based biological diesel oil comprises 10-20% methanol, 0.5-2% n-butyl alcohol, 0.1-2% tert-butyl alcohol, 0.1-2% cyclohexamine, 10-15% cooking oil or vegetable oil acid, 0.1-2% liquid paraffin, 1-5% petroleum benzene, 0.0006-0.003% isooctyl nitrate and 40-60% petrochemical diesel oil. Preparation of alcohol-based biological diesel oil comprises stirring uniformly raw materials until transparent.    USE - Alcohol biological diesel oil, and its preparation (claimed).
NOVELTY - Preparation of tobacco stem biomass carbon for killing snail comprises taking tobacco stem, naturally drying to less than 16 wt.% water content, crushing into 2-10 mm; taking dried tobacco stem into biomass carbonizing furnace and carbonizing under high temperature; cooling and sieving in 40-60 mesh sieve to obtain 72.8-98.3 mg/m2 tobacco biomass carbon; and adding to water to kill snails.    USE - Method for preparing tobacco stem biomass carbon for killing snail (claimed).    ADVANTAGE - The method is simple, easy to operate and utilizes waste. The production cost is low. The biomass carbon can kill snails in 3 days.
NOVELTY - Recycling wastewater from thiazoximic acid production involves oximating and methylating wastewater, hydrolyzing to dissolve sodium nitrite, reacting with ethyl acetoacetate, finishing oximation, adding soda ash, methanol and dimethyl sulfate, layering, extracting, distilling, recovering extracting agent and solvent, and discharging wastewater; hydrolyzing, adding deionized water to dissolve cyclization ester, adjusting pH, adding complexing, bleaching and auxiliary bleaching agents, filtering and centrifuging; and leaching residue, drying, centrifuging filtrate, washing, and returning to oximation reaction.    USE - Recycling wastewater from thiazoximic acid production (claimed).    ADVANTAGE - The method reduces the wastewater discharge, greatly improves production yield and wastewater discharge technique, and has better economic and environmental protection benefits.    DETAILED DESCRIPTION - Recycling wastewater from thiazoximic acid production oximating and methylating wastewater, hydrolyzing to dissolve sodium nitrite, reacting with ethyl acetoacetate, finishing oximation, adding soda ash, methanol and dimethyl sulfate, layering, extracting reaction product from wastewater, distilling, recovering organic extracting agent, recovering solvent, and discharging wastewater; hydrolyzing, adding deionized water to dissolve cyclization ester and adjusting pH, adding complexing agent, bleaching agent and auxiliary bleaching agent, filtering, and centrifuging; and leaching residue, drying to obtain dried product, centrifuging filtrate, washing with water, and returning back to oximation reaction.
NOVELTY - The reactor has a closed digester provided with municipal waste. The waste is warmed and moistened with warm water that is sprayed through nozzles. The temperature in a reactor body is increased by energy that is recovered by engine cooling co-generation. Biogas is formed in a combustion chamber. A lower chamber is filled with fermenting material. An upper chamber is provided with a device hoppers and a horizontal feeder. An end of a tray is provided with a two-step valve, which changes flow direction of charged materials.    USE - Compact reactor for fermentation of municipal waste.
NOVELTY - The method involves feeding first stage raw waste water (1) to an anaerobic reactor (2), and removing carbon pre-compounds by a methane fermentation process to produce biogas. A purification step is performed using a chemical precipitation of phosphorus in a reactor (4). Nitrogen is removed from the waste water in a biological reactor (9), and the waste water is cleaned using sand filters (10). The treated waste water (11) is discharged to a receiver. Excess sludge (12) is discharged into the anaerobic reactor for stabilization, and the sludge is dewatered.    USE - Municipal waste water treating method for removing nitrogen compounds.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a municipal waste water treating method.    Raw waste water (1)    Anaerobic reactor (2)    Reactor (4)    Biological reactor (9)    Sand filters (10)    Treated waste water (11)    Excess sludge (12)
NOVELTY - System comprises a digester (1) that is supplied with organic raw material through an inlet pipe (2) and diluted with water produced through anaerobic digestive biofertilizer. The organic raw material is collected in an outbox (3) and biogas chamber, where the biogas is sent to a gasometer (7) that equalizes the biogas and maintains constant pressure to feed an electric motor or generator (15), which runs on biogas. The motor or generator feeds the electric charge unit (17) and a stove (21) for cooking food. The biogas is generated in the digester.    USE - System for continuous monitoring of biodigestion efficiently (claimed).    ADVANTAGE - The system produces biofertilizer utilized by farmers.    DETAILED DESCRIPTION - All elements of the plant are monitored and controlled continuously by a computer program installed on a personal computer of a control panel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system.    Digester (1)    Inlet pipe (2)    Outbox (3)    Gasometer (7)    Control panel (11)    Electric motor or generator (15)    Electric charge unit (17)    Stove (21)
NOVELTY - Manufacture of biofuel involves thermally-decomposing wood material.    USE - Manufacture of biofuel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofuel.
NOVELTY - Producing biogas use as biofuel involves fermenting prickly pear cacti in a digester with hot water and nopal at 35-40 degrees C at pH 6.9-7 in presence of bacteria. A feed hopper is provided for moving raw material through a lift to a feed pump and then to a filter. A water supply valve is connected to the anaerobic digester or reactor, which includes a heat exchanger and two pumps.    USE - Method for producing biogas used as biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for producing biogas.
NOVELTY - Manufacture of biomass fuel involves crushing palm shell, performing rough grinding of the resultant crushed palm shell, obtaining palm shell mixture, adding coal, mixing uniformly, molding to a predetermined shape, and packing.    USE - Manufacture of biomass fuel (claimed).    ADVANTAGE - The method economically provides biomass fuel having excellent durability and stability for a long period of time, by suppressing the generation of toxic gas.
NOVELTY - A lignocellulosic biomass liquefaction method involves mixing ground biomass in solution including liquid solvent and 10-50 wt.% catalyst containing acid, heating the mixture at temperature of 260-400 degrees C and pressure of 30-80 bar to form fraction of liquid and gas, contacting the mixture with a catalyst, removing and cooling the liquid biomass, and separating reaction gases for 10 seconds to 2 hours.    USE - Method for liquefying lignocellulosic biomass.    ADVANTAGE - The method enables liquefying the lignocellulosic biomass in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for installing liquefied lignocellulosic biomass.
NOVELTY - Producing biodiesel involves carrying out the transesterification of alcohol and oil by using enzymes in microgravity for 12-36 hours in order to separate the biodiesel material. The microgravity is obtained by using clinostat. The transesterification is performed at 10-30 degrees C. The enzymes are obtained form selected from Candida rugosa, Candida antarctica, Aspergillus niger, Rhizopus niveus, Pseudomonas fluorescens, Mucor javanicus or Burkholderia cepacia.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables to produce biodiesel efficiently.
NOVELTY - Producing bioethanol involves treating banana pseudostem in ultrasonic bath for 3 hours at a temperature of 60 degrees C. The obtained material is treated with sulfuric acid or peracetic acid and sodium hydroxide. The obtained materials are then treated again in an ultrasonic bath. The obtained materials are hydrolyzed in presence of cellulose enzyme and sodium acetate buffer and yeast for 4-5 hours at pH 4.8. The percentage of lignin and hemicellulose and cellulose in the banana pseudostem is determined by neutral detergent fiber.    USE - Method for producing bioethanol from pseudostem of banana.    ADVANTAGE - The method enables to produce bioethanol from pseudostem of banana efficiently.
NOVELTY - A solid material is removed from a palm byproduct by filtration, after raising the temperature of the palm byproduct. An organic solvent is added to the palm byproduct and dissolved at 25-35 degrees C. Moisture is removed by contacting the palm byproduct with moisture scavenger. Impurities and the organic solvent are removed from the palm byproduct without moisture to obtain a refined palm byproduct. Fatty acid contained in the refined palm byproduct is subjected to ketonization reaction, to obtain ketone compound. The ketone compound is hydrodeoxygenated to obtain parrafin.    USE - Manufacture of paraffin (claimed) used as biofuel.    ADVANTAGE - The method enables manufacture of paraffin with low sulfur content by environmentally-friendly process, using palm byproduct as raw material.
NOVELTY - Refrigerant composition comprises (in wt.%): 1,1-difluoroethane (15-25); 2,3,3,3-tetrafluoropropene (45-55); isobutane (15-25); and cyclopropane (5-15).    USE - The Refrigerant composition is useful for automobile air conditioner (claimed).    ADVANTAGE - The refrigerant composition can be economically prepared in an eco-friendly manner with low atmosphere pressure state, excellent vaporization latent heat, and low solidifying point, excellent volume cooling capacity, high critical temperature, low viscosity, and excellent heat transfer performance and electrically insulating property.
NOVELTY - The tubular reactor includes using organic waste as energy resources for reactor operation, where the reactor allows separation of stages of production process of methane in a single reactor automatically. Main transport phenomenon is diffusivity of the material inside the reactor.    USE - Tubular reactor for production of methane from anaerobic digestion of organic matter.
NOVELTY - Use of modified two-stage activated sludge processing method for treating nitrate-polluted drinking water comprises adding raw water into titanium dioxide (TiO2) modified denitrifying activated sludge reactor (2); carrying out sequencing batch operation process, and controlling carbon source adding amount with partial reduction of part of nitrate; draining in second sludge reactor and carrying out denitrification treatment; adding carbon source and heterotrophic hydrogen to completely reduce the nitrate and nitrite to nitrogen; precipitating; and sterilizing and activated carbon filtering.    USE - Method of using modified two-stage activated sludge processing for treating nitrate-polluted drinking water.    ADVANTAGE - The method provides environmental protection.    DETAILED DESCRIPTION - Use of modified two-stage activated sludge processing method for treating nitrate-polluted drinking water comprises:    (A) adding raw water into TiO2 modified denitrifying activated sludge reactor (2);    (B) carrying out sequencing batch operation process, and controlling carbon source adding amount with partial reduction of part of nitrate in raw water;    (C) draining in second TiO2 modified denitrifying activated sludge reactor, and carrying out denitrification treatment with denitrification synergistic effect;    (D) completely adding carbon source and heterotrophic hydrogen to completely reduce the rest nitrate and nitrite to nitrogen;    (E) introducing raw water into sedimentation tank (4) to carry out precipitation treatment; and    (F) then sterilizing by ozone and activated carbon filtering to obtain drinking water.    An INDEPENDENT CLAIM is included for a device for production of hydrogen with electrolysis including TiO2 modified active mud reactor (3), sedimentation tank (4), ozone sterilizing and activated carbon filter tank (5), water tank (6), treatment tank (7), hydrogen electrolysis device (9) and air pressure adjusting bag (10).
NOVELTY - The system has a heat transfer unit for transferring heat using a heat source and circuit unit. A heat exchanger element is coupled to the circuit unit and attached to a surface of a delimiting wall. An outer wall is provided with an insulation element. Two heat exchangers are detachably coupled in a series. The heat exchanger element is used for collecting heat. A shape of the heat exchanger element is changed depending on the shape of an attaching surface.    USE - Heat transfer system for biogas production plant.    ADVANTAGE - The system is processed with low percentage of protein or carbohydrate, and simple to process.
NOVELTY - The well (14) has a pre well (12) for storing organic material, and a post well (16) for storing store digested residue from a digester (24) that is provided inside a biogas production plant system (1). The pre well and the post well are separated by a well heat conducting partition (160). The warm digested residue in the post well forms a mantle around the cold incoming organic material in the pre well. A recovery system is provided with a heat pump that is provided with two media circuits.    USE - Combined pre and post well for use in biogas production plant.    ADVANTAGE - The biogas production plant with combined pre and post well has high energy efficiency, thus saving production costs and energy resources, and minimizing the amount of heat produced during biogas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biogas production plant that is provided with a combined pre and post well.    Biogas production plant system (1)    Pre well (12)    Combined pre and post well (14)    Post well (16)    Digester (24)    Well heat conducting partition (160)
NOVELTY - B5 biological diesel fuel blend comprises 94-95 vol.% no.0 diesel oil, 2-4 vol.% levulinic acid ethyl ester, 1-3 vol.% diesel oil, 0.03-0.05 vol.% cosolvent, and 0.01-0.05 vol.% cetane number improving agent.    USE - B5 biological diesel fuel blend used for diesel engine vehicle.    ADVANTAGE - The physical and chemical properties and dynamic performance satisfies GB/T25199-2010 for biodiesel blended fuel (B5). The combustion in diesel engine reduces soot, carbon monoxide, carbon dioxide, and nitrogen oxide pollutant discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing B5 biodiesel oil comprising mixing levulinic acid ethyl ester, mixing uniformly to form mixed liquid, then adding cosolvent, and cetane number improving agent to obtain mixture, then stirring mixture into no.0 diesel oil to obtain mixed fuel.
NOVELTY - Preparing hydrocyanic acid derivative using coke-oven gas, comprises performing variable pressure absorption of the coke-oven gas and then separating with low quality methane gas, carbon monoxide, hydrogen and tail gas, processing methane gas as the raw material to produce certain amount of hydrogen and carbon monoxide, performing hydrogenation on the methane gas to obtain hydrogen derivatives or liquid ammonia, and synthesizing carbon dioxide and tail gas to obtain methanol and formaldehyde for absorbing hydrocyanic acid to prepare hydroxyl acetonitrile.    USE - The method is useful for preparing hydrocyanic acid derivative using coke-oven gas (claimed).    DETAILED DESCRIPTION - Preparing hydrocyanic acid derivative using coke-oven gas, comprises performing variable pressure absorption of the coke-oven gas and then separating with low quality methane gas, carbon monoxide, hydrogen and tail gas, processing methane gas as the raw material to produce hydrocyanic acid derivative and certain amount of hydrogen and carbon monoxide components, performing hydrogenation on the methane gas to obtain hydrogen derivatives or liquid ammonia, producing hydrocyanic acid using a synthetic ammonia device, and synthesizing a carbon dioxide and tail gas to obtain methanol and formaldehyde for absorbing hydrocyanic acid to prepare hydroxyl acetonitrile.
NOVELTY - Method for synthesizing major peptide fragment of formula: Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OH (I) of somatostatin, involves (a) reacting Lys(Boc)-OX or its salt with Fmoc-Cys(Trt)-OH to obtain Fmoc-Cys(Trt)-Lys(Boc)-OX, (b) removing Fmoc protecting group from Fmoc-Cys(Trt)-Lys(Boc)-OX to obtain Cys(Trt)-Lys(Boc)-OX, (c) reacting Cys(Trt)-Lys(Boc)-OX and Boc-Ala-Gly-OH to obtain Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OX, and performing hydrolysis reaction of Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OX to obtain Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OH.    USE - The method is useful for synthesizing major peptide fragment of somatostatin which is used as synthetic intermediate (all claimed).    ADVANTAGE - The method enables to increase peptide coupling yield effectively, shorten peptide coupling time and improve peptide purity. The method has mild reaction conditions, is simple as reagents are cost-effective and easy to obtain, and avoids use of hydrogenation or expensive and non-environmentally-friendly reagents.    DETAILED DESCRIPTION - Method for synthesizing major peptide fragment of formula: Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OH (I) of somatostatin, involves (a) reacting Lys(Boc)-OX or its salt with Fmoc-Cys(Trt)-OH to obtain Fmoc-Cys(Trt)-Lys(Boc)-OX, (b) removing Fmoc protecting group from Fmoc-Cys(Trt)-Lys(Boc)-OX to obtain Cys(Trt)-Lys(Boc)-OX, (c) reacting Cys(Trt)-Lys(Boc)-OX and Boc-Ala-Gly-OH to obtain Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OX, and performing hydrolysis reaction of Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OX to obtain Boc-Ala-Gly-Cys(Trt)-Lys(Boc)-OH, where the X is lower alkyl group, or substituted or unsubstituted phenyl group.
NOVELTY - Glycerol is contacted with a catalyst (10) under high temperature and pressure to directly produce a mono-oxygenated compound.    USE - Direct production of mono-oxygenated compound from glycerol obtained by by-product from transesterification of biodiesel production.    ADVANTAGE - The method enables production of mono-oxygenated compound with high reaction rate and product purity, in a single-step hydrogenation reaction, bypassing a precursory dehydrating step (producing an intermediate product, such as acrolein). The method enables quick and economical conversion of glycerol to an alcohol which can then be recycled back to the biodiesel production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for catalyst comprising particles of at least one transition group metal bound to support (12) in a concentration of 0.5-5 wt.% based on the weight of support.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the method for producing catalyst.    Catalyst (10)    Support (12)    Distilled water (14)    Support paste (16)    Catalytic solution (18)
NOVELTY - A kind of window-shades type large area cold plasma waste gas processing device, comprising a plasma shell body, the inner cavity of at least one cross section is set with several plasma generator, the same cross section a plasma generator of the edge cross section and filled, plasma generator vertical shell body gas inlet, a plasma generator comprising an insulating base, the front and back are respectively connected with air flow uniformly distributing grid, a base inner cavity between the left and right sealed from up to down vertically is connected with several the first end of the insulating medium tube, the insulating medium tube are set on the same base in the cross section, the insulating medium tube adjacent the closed end in the left and right are set in the insulating medium tube are matched electrode, each electrode one end of which is connected with the electrode wire, the base left and right electrode wire is respectively connected with the high voltage alternating current power supply voltage end of the first pin; The utility model can obtain higher process gas flow rate, which can keep high density large area plasma discharge process in steady-state and improve the processing efficiency and reduce the energy consumption.
NOVELTY - Phloroglucinol wastewater recovery treatment method involves extracting phloroglucinol wastewater using methyl isobutyl ketone to obtain a methyl isobutyl ketone solution containing organic substance having phloroglucinol, and an inorganic aqueous solution containing potassium chloride, distilling methyl isobutyl ketone solution to reclaim methyl isobutyl ketone extraction agent, producing phloroglucinol, and performing evaporation and salt separation of inorganic aqueous solution to obtain byproduct potassium chloride and remaining wastewater.    USE - Phloroglucinol wastewater recovery treatment method (claimed).    ADVANTAGE - The reclamation rates of phloroglucinol and potassium chloride is more than 90%. The extraction agent and condensing water are recycled economically.
NOVELTY - The device has a carbonization chamber provided with a rotary sleeve (4) that is connected with a rotating wheel (1). A cloth roller is connected with a lower part of the rotating sleeve. An inner rotating sleeve is provided with a rotating shaft that is supported by a supporting shaft sleeve (11). A lower part of the supporting shaft sleeve is connected with a carbon scraping knife (10). A carbon tool retainer plate is fixed with a lower end of a conical carbon discharging hopper (13) that is fixed with a discharge valve (14). The discharging valve is connected with an external device (15).    USE - Biomass dense forming particle based efficient carbon gasification comprehensive pyrolysis device.    ADVANTAGE - The device provides tar and pollutionless gas, and has high thermal efficiency. The device realizes a multi-stage utilization that makes full usage of resource and energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass dense forming particle based efficient carbon gasification comprehensive pyrolysis device.    Rotating wheel (1)    Rotary sleeve (4)    Carbon scraping knife (10)    Supporting shaft sleeve (11)    Conical carbon discharging hopper (13)    Discharge valve (14)    External device (15)
NOVELTY - A kind of straw gasification furnace, comprising a furnace body, a storage section, a gas in the furnace body. the lower part is combustion zone, wherein the upper part of the furnace body surrounding the furnace body is provided with air storage chamber, and the gas storage chamber and the storage area with a through hole, inner wall of the furnace body is fixed with a branch connected with the air storage chamber is a water discharge pipe, the other end of the oil-water discharge pipe connected with the combustion area, an air inlet connected with the air chamber of the gas downlink pipe. This utility model is a kind of straw gasification furnace is provided with an annular gas storage chamber at upper part of the furnace body, and is provided with a gas storage chamber is connected with the combustion zone and a water discharge pipe, a majority of tar in the gas of the to the combustion area, reduces the pollutant discharge the indoor air condensation. Gas pipe is set on the air downwards in the hearth, the temperature in the furnace is high, even if there is a little tar will not form blockage in the tube.
NOVELTY - This utility model claims a kind of straw gas making furnace. The straw gas furnace comprises a furnace body, a washer, cooling and filtrating box, a dust remover, a blower and a gas storage cabinet, wherein the furnace body is a furnace cavity, the furnace cavity is provided with a circle of cooling water jacket, the lower part of the furnace chamber is provided with a furnace ash chamber, the washer through the connecting pipe with the furnace ash chamber is connected to the cooling and filtrating box through the connecting pipe and the washer is connected with the dust remover through the connecting pipe and the cooling and filtrating box is connected with the dust remover through the connecting pipe and the air blower I is connected with one end, the other end of the fan is provided with a water seal tank and a gas storage cabinet and the water seal tank through the connecting pipe is respectively connected with the blower and the air storage cabinet is connected with the side wall of the gas storage cabinet is provided with an air delivery pipe. This utility model claims a kind of simple structure, high heat utilization ratio of straw gas making furnace.
NOVELTY - This utility model claims a kind of spherical biomass fuel forming machine, comprising a base, a machine frame, a main die roller, mould roll, a horizontal material pushing device, a vertical material pushing device, a hopper, a discharge sliding groove and a transmission device. The machine seat is fixedly provided with rack, a horizontal pushing raw material through one end of the bearing seat is fixed on the machine frame, the shaft end set with a transmission belt pulley is fixed provided with a feeding hopper, the other end is connected with the first vertical raw material pushing device is fixedly connected with the vertical raw material propulsion device of one end of the bearing seat is fixed on the machine frame, the shaft is set on the upper end of transmission belt, the other end an outlet end corresponding to the main die roller, an auxiliary die roller connected with the main and assistant die roller is fixed under a discharging sliding groove. This utility model reaches the low output, high pressure, electricity-saving, consumption-reducing effect, the old a day section 80KW, annual can save 13 ten thousand kwh, saves 10 of investment , can make full use of straw, rice hull, sawdust, coal and so on waste compressing into spherical solid fuel.
NOVELTY - The utility model claims a sewage treatment plant dewatered sludge with kitchen waste grease resources distributed processing system, comprising a sludge storage tank and kitchen waste oil storage tank, sludge storage tank is connected with condensed conditioning agent feeding device, a sludge storage tank is orderly connected with a stirring and filter plate compacting device and a dewatering chamber, kitchen waste filtering system is connected with the oil storage tank, hydration degumming stirring tank and desulphurizing device, chamber processing tank is connected with a mud, desulphurization device is connected with kitchen waste grease processing tank, a processing tank for sludge and kitchen waste grease processing tank is respectively connected with the sludge crushing and mixing system is connected with the sludge crushing and mixing system outlet is connected with a press device, press device and discharging conveying system, the invention has the following advantages: simple technique, the operation is convenient, the cost is low, energy-saving and environment-friendly, providing a some waste into valuable feasible way for a large amount of city sludge and using oil.
NOVELTY - The boiler has a circulating fluidized bed gasification furnace provided with a lifting pipe, a cyclone separator and a cyclone dust collector. A gas boiler unit is provided with a hearth and a heating surface. A side wall of the lifting pipe is provided with a feeding port. A biomass raw material is entered into the lifting pipe from the feeding port. The hearth is utilized for providing generated gas by the cyclone separator. The cyclone dust collector is connected with a heat source.    USE - Biomass gasified combustion boiler.    ADVANTAGE - The boiler is simple in structure, and improves product quality, avoids alkali metal corrosion and prevents heating area accumulating dust. The boiler has better temperature resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasified combustion boiler.'(Drawing includes non-English language text)'
NOVELTY - The method involves entering a mixed refrigerant into a compressor. The mixed refrigerant is put into an outlet cooler to obtain a mixed coolant. The mixed coolant is continuously entered into a mixed coolant compressor outlet cooler. The mixed coolant is passed into a cold tank inlet separating tank. Gas is flowed to a cold box system through a top part. A mixed refrigerant liquid phase is entered into the cold box system. The mixed coolant is made of nitrogen or methane or ethylene or ethane or propane or propylene or butane and pentane.    USE - Single-circulating refrigerant compression and conveying method.    ADVANTAGE - The method enables providing simple and easy operation, reducing manufacturing cost of a cooling agent pump, the cooler and a buffer tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a single-circulating refrigerant compression and conveying system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a single-circulating refrigerant compression and conveying system. '(Drawing includes non-English language text)'
NOVELTY - A kind of heat supply are dual catalytic reactor, comprising a reactor (R1), the second reactor (R2), a first heat exchanger (E1) and the second heat exchanger (E2), wherein the first reactor (R1) and the second reactor (R2) and the first heat exchanger in the heat exchanger (E1) and the second heat exchanger (E2) are set in the same shell body (R), wherein the shell (R) is further provided with a first heat exchanger (E1) and the second heat exchanger (E2) are connected in series and connected with the first reactor (R1) to the second reactor (R2) waste heat or the second reactor (R2) to the first reactor (R1) of waste heat supply heat exchanger (E3). This utility model passes through to a plurality of other heat supply reactor in a reactor, it cancels the external heat supply system, simplifies the device and pipeline, so that the whole process compact and effective, the operation is more safe.
NOVELTY - This utility model is one kind of bi-level transmission belt type biomass briquetting machine. Power device is a pressing block mechanism is mainly composed of a motor, a transmission belt wheel, a transition transmission shaft, a second transmission belt wheel and the main shaft, transmission belt wheel are corresponding to each other are formed by the large diameter triangular belt wheel and the triangular belt pulley. The output shaft of the motor is provided with small diameter triangular belt wheel of first stage transmission belt wheel set, and a large diameter triangular belt pulley is set on the transitional transmission shaft section, the triangular belt wheel of the second stage transmission belt group is set on the transitional transmission shaft section, and the large diameter triangular belt pulley is set on the main shaft. This utility model adopts the single electric motor and machine a according to matched with the double-motor machine power saving without energy waste, wherein the secondary transmission belt pulley, the machine has more stable and the operation power, simple structure, small operating noise and convenient maintenance.
NOVELTY - A circulating fluidized bed boiler fly ash and bottom ash to obtain synthetic zeolite involves carrying out decarburization treatment, after mixing the fly ash and bottom ash, and fine grinding by a ball mill for ash to obtain mixed powder; mixing the powder, adding alkali solution to it, to obtain mixed solution; stirring to make crystal; filtering, and washing the crystals till the pH is equal to 9-10, and then filtering, discarding the washing solution, and collecting crystal to obtain zeolite.    USE - As a circulating fluidized bed boiler fly ash and bottom ash to obtain synthetic zeolite, which is used in agricultural soil, fertilizer and environment protection field.    ADVANTAGE - The process provides zeolite having high cation exchange capacity, and high specific surface area; and effectively protects the ecological environment.    DETAILED DESCRIPTION - A circulating fluidized bed boiler fly ash and bottom ash to obtain synthetic zeolite involves carrying out decarburization treatment, after mixing the fly ash and 20-30 wt.% bottom ash, and fine grinding by a ball mill for ash, to obtain mixed powder; mixing the obtained powder, adding alkali solution to it, to obtain mixed solution; stirring at 50-70 revolution/minute for 1-2 hours at 95-100 degrees C, and at 20-40 revolution/minute for 4-6 hours at 95-100 degrees C, to make it crystal; filtering, and washing the crystals till the pH is equal to 9-10, and then filtering, discarding the washing solution, and collecting crystal at 85-100 degrees C for 3-5 hours to obtain zeolite product, where the alkali solution is sodium hydroxide (NaOH) solution whose concentration is 2.5-3.2 mol/l.
NOVELTY - Fertilizer comprises 30-50 pts. wt. of solid waste organics, 30-50 pts. wt. of glutathione, 1-8 pts. wt. of inorganic nitrogen, phosphorus, and potassium (NPK) nutrients, 1-2 pts. wt. of solubilizing strains and 5-10 pts. wt. of filler, where: the solid waste organics comprises mushroom residue, furfural residue, plant ash, clover slag; NPK nutrients comprise urea, ammonium phosphate, potassium chloride or potassium sulfate; and the solubilizing strains comprise Bacillus megaterium, Escherichia coli, Bacillus mucilaginosus, or Pseudomonas fluorescens.    USE - Used as fertilizer.    ADVANTAGE - The fertilizer can be economically prepared with high efficiency in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising placing the solid waste organic matter and glutathione and then mixing, adding solubilizing strains and then fermenting into a solid fermentation at normal temperature to obtain a product and then crushing, and adding inorganic NPK nutrients and filler into pelletizer and then spraying and packing.
NOVELTY - 7-chloro-5-oxo-2,3,4,5-tetrahydro-1H-1-benzoazepine carboxylic acid ester (I) is new.    USE - For treating congestive heart, liver cirrhosis and antidiuretic kinase secretion syndrome caused by low sodium hyperlipidemia.    ADVANTAGE - The benzoazepine carboxylic acid ester is prepared by a one-pot method, which simplifies the reaction operation, the raw material and reagent is cheap, the reaction is mild and environment-friendly, it is suitable for mass production.    DETAILED DESCRIPTION - 7-chloro-5-oxo-2,3,4,5-tetrahydro-1H-1-benzoazepine carboxylic acid ester of formula (I) is new.    R=phenyl, benzyl (optionally substituted), or 1-6C alkyl.    An INDEPENDENT CLAIM is included for preparation of 7-chloro-5-oxo-2,3,4,5-tetrahydro-1H-1-benzoazepine carboxylic acid ester (I).
NOVELTY - An oxygen-enriched biomass circulating fluidized-bed gasification system has a gasification furnace filled with biomass and oxygen-enriched air that is pre-heated by a pre-heater. Overheated steam enters into the gasification furnace, and the biomass is fluidized under the action of a bed material. The high temperature fuel gas is subjected to gas-solid separation. Residual carbon in the fuel gas and bed material is fed into the furnace. High temperature fuel gas is separated from the system through a cyclone dust collector, an over-heater, a waste heat boiler and the pre-heater.    USE - Oxygen-enriched biomass circulating fluidized-bed gasification system.    ADVANTAGE - The system reduces volume fraction, dust and coke oil concentration in the fuel gas and improves thermal value, and has high quality.    DETAILED DESCRIPTION - An oxygen-enriched biomass circulating fluidized-bed gasification system comprises biomass fed from lower part of a gasification furnace and oxygen-enriched air pre-heated by a pre-heater. Overheated steam enters into the gasification furnace, and the biomass is fluidized under action of a bed material to generate pyrolysis and gasification reactions. The high temperature fuel gas is subjected to gas-solid separation by using a cyclone separator. Residual carbon in the fuel gas and the bed material are fed into the gasification furnace. The high temperature fuel gas is separated from system through a cyclone dust collector, over-heater, a waste heat boiler and the pre-heater, where temperature of the oxygen-enriched air and the superheated steam in the gasification furnace is controlled at 650-950 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an oxygen-enriched biomass circulating fluidized-bed gasification system.'(Drawing includes non-English language text)'
NOVELTY - A biomass gas purifying and cooling method involves removing fly ash in biomass gas through a cyclone dust collector, and transporting the biomass gas to a tar cracking device and a combustion improver to perform combustion reaction for supplying heat to cracking tar, and splitting the tar into small endothermic gas molecules. Waste heat in high-temperature gas is recycled with a gasification agent and water, and temperature of the biomass gas is reduced to 100-150 degrees C. Fly ash in the biomass gas is removed by a bag type dust collector. The biomass gas is cooled by an air-water cooler.    USE - Method for purifying and cooling biomass gas.    ADVANTAGE - The method enables thoroughly removing the fly ash in the biomass gas, splitting the tar into small endothermic gas molecules and avoiding secondary pollution generation.    DETAILED DESCRIPTION - A biomass gas purifying and cooling method involves removing fly ash in biomass gas generated by a gasification furnace through a cyclone dust collector, and transporting the biomass gas to a tar cracking device and a combustion improver to perform combustion reaction for supplying heat to cracking tar, and splitting the tar into small endothermic gas molecules. Waste heat in high-temperature gas is recycled with a gasification agent and water, and temperature of the biomass gas is reduced to 100-150 degrees C. Fly ash in the biomass gas is removed by a bag type dust collector. The biomass gas is cooled to temperature less than 50 degrees C by an air-water cooler.
NOVELTY - This utility model claims a three-segment from guide groove of bulk waste matter through continuous pyrolysis and gasification furnace, the pyrolyzing gasification furnace top is provided with a power assembly is set on the lower section of the furnace body, the power assembly is set on the middle section of the furnace body on the lower section furnace body, wherein the upper section of the middle section of the furnace body, the furnace body is provided with a material pressing device on the upper part of the furnace body, the pressing device is provided with a furnace cover, the upper section of the furnace body is provided with a feeding device. This utility model solves the existing technology in waste incineration in the process difficult technical problem, using the new bulk garbage combustible through continuous pyrolysis and gasification furnace, burning can the same reduction effect is good, but also will not image burning caused by soot, especially produce.
NOVELTY - N-((S)-1-((R)-1-(Difluoroboryl)-3-methylbutylamino)-1-oxo-3-phenylpropan-2-yl)pyrazine-2-carboxamide (I) as bortezomib key intermediate is new.    USE - As bortezomib key intermediate for synthesis of bortezomib (claimed) as anti-tumor medicine for treating multiple myeloma blood cancer, mantle cell lymphoma and other B cell type lymphoma.    ADVANTAGE - The compound (I) is used as high purity bortezomib by key intermediate, used to synthesize high purity bortezomib by bubble and the hydroxylation reaction with low production cost. The method is simple and is friendly to the environment, and is very easy for industrial production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of the compound (I); and    (2) synthesis of bortezomib involving: reacting the compound (I) at -30 to 100, preferably -10 to 80 degrees C, in the reaction solvent to obtain the bortezomib by hydroxylation reaction.
NOVELTY - A kind of horizontal pushing vertical biomass carbon gas-oil-joint device, by means of a horizontal pushing device makes the biomass laminated back to move downwards in the vertical pyrolysis furnace, a gas heat-carrying medium directly passes through the material layer, a heat of biomass in the form of direct current, specific structure comprises an external furnace body and the furnace body for baking basic steel ladle furnace lining surrounded by dry distillation reaction space, dry distillation reaction space a is divided into approximately equal to six layers of horizontal case space, the six-layer space is divided into three area, moisture removal region, low temperature pyrolysis area, a high temperature pyrolysis area, horizontal fire grate is provided with a layer of a horizontal box body space in a plurality of times of back-turning way. This utility model realize the physical sub-area of the pyrolysis process, it can adjust the carbonization process is greatly improved, pyrolysis product fast separating speed and material layer, product yield of liquid product, a draught fan power consumption is greatly reduced, the cost is reduced, the utility model is of vertical arrangement, small floor area, easy to realize multi-set in parallel.
NOVELTY - A kind of Groove cross fork flow biomass dry distillation tower, comprising a biomass raw material bin (1), a drying section, section, a cooling chamber (6) and smoke gas processing system, a drying section including a drying tower (2) and a drying tower (3), the upper part of the dry distillation section comprising distillation tower (4) and a dry distillation tower (5), the raw material bin (1), a drying tower (2), a drying tower (3), a distillation tower (4), a distillation tower (5) and a cooling chamber (6) from the top to bottom are connected, gas processing system connected with each inlet and outlet drying section and distilling section. Inner part is provided with multiple groups of dry distillation tower for biomass producing hydrogen and ethanol through the vertical groove channel unit, between any two groups of groove channel unit comprising a space for heat smoke rises horizontally to pass through, the vertical groove channel unit section is " Z "-shaped heat transfer element are combined with each other; This utility model improves the production efficiency, high heat energy utilization rate, small equipment volume; with direct heating mode and the indirect heating method, the utility model heat transfer element for heat-resisting material, long service life and low price.
NOVELTY - The utility model claims a van-type biomass solid fuel production line, belonging to the technical field of agricultural machinery. The production line comprises a traction moving of along the length direction orderly arrange crusher, conveyor, a cyclone bin and the machine room, the output end of the grinder is connected with the inlet of the conveying fan, the outlet of the fan is connected with the inlet of the cyclone hopper, the outlet of the cyclone hopper connecting the inlet of the granulating machine by a spiral conveyor. When working, the utility model can develop under the driving of the traction machine, which is convenient to the field or straw head is stored, the substantially dry straw input to the crusher, crushing into particle having a predetermined length, and is pumped in a cyclone hopper conveyor, which not only realize gas-solid separation, and further drying, cyclone at the bottom of storage bin of dry crushed material under the action of the spiral conveyer, the granulator, compressed into granules, can use the biomass solid particle fuel, so as to lay the foundation for further use.
NOVELTY - This utility model claims a kind of saving energy and reducing consumption, a cracking furnace and a furnace main body of the cracking furnace is provided with a hopper, and the cracking furnace comprises a fuel gas pipe connected with the cracking furnace and combustion hearth, a furnace body connected with the combustion hearth. Through said method, the utility model can solve the problem that the hearth of fuel combustion is not complete, resulting in thermal efficiency is low, the smoke generated in the process contains a large amount of dust, no problem of environment-friendly and energy-saving, comprising biomass combustion is more complete, improves the heat efficiency and purifying gas and energy-saving environment-friendly and so on.
NOVELTY - This utility model claims a combustible gas detecting warning device, wherein the combustible gas detecting and alarming device comprises a single chip, the input end of the single chip computer is connected with a sensor, the output end of the single chip is connected with an LCD display, a relay and a buzzer, the relay and the other end is connected with an air discharge device. This utility model can detect the inner air liquefied gas is a dangerous, hydrogen and a hazardous gas is propane, at the same time, also can be displayed at that time is the concentration of hazardous gas on the LCD, but also can send out alarm, and then to release the danger by the relay of controlling an exhaust unit, which satisfies the demand of the people.
NOVELTY - The method involves containing a graphite particle and a thermosetting resin component. A molding material is prepared in the ratio of the graphite particle with respect to the solid content in the range of 70-90 mass percent. A separator (20) is produced by molding the molding material. A gasket (12) is laminated on the separator. A blasting is given to the separator after the gasket is laminated on the separator. A hydrophilization treatment improves hydrophilic property of the surface given to the separator after the blasting.    USE - Method for manufacturing a separator (claimed) for fuel cells i.e. polymer electrolyte fuel cell.    ADVANTAGE - The method enables equipping the separator with the gasket, so that the hydrophilic property of the surface of the separator is high, thus obstructing the groove for gas supply emission in the separator. The method enables adjusting the static contact angle with the water of the surface of the separator by setting the conditions of the hydrophilization treatment. The detachment of the metal ion from the separator within the fuel cell is suppressed, so that the fall of the electrolytic proton conductivity and electrolytic disassembly are suppressed, thus maintaining performance of the fuel cell over a long term.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a separator.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective views of a separator.    Groove (2)    Gasket (12)    Opening (15)    Separator (20)    Fuel electrode (32)
NOVELTY - Processing (M1) a biomass fuel compact, comprises: combining a composition of combustible biomass materials; comminuting the composition of biomass materials; rotary friction drying of biomass materials; adding an adhesive comprising starch and hydroxide to the biomass materials to form a composite biomass; forming the composite biomass into a shapeform; and heat treating composite biomass shapeform at a base temperature to break oxygen-hydrogen bonds, where the base temperature is below a torrefaction temperature of composite biomass so that torrefaction of biomass materials does not occur.    USE - The method is useful for processing a biomass fuel compact (claimed).    ADVANTAGE - The method: is cost-effective and eco-friendly; and provides highly durable biomass fuel compact having moisture resistant, and which significantly reduces the traditional dust issues associated with the conventional biomass compositions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (M2) for processing a biomass fuel compact, comprising heat treating biomass materials of the biomass fuel compact at a base temperature to break oxygen-hydrogen bonds, where the base temperature is below a torrefaction temperature of the biomass fuel compact so that torrefaction of the biomass materials does not occur;    (2) a biomass fuel compact manufactured according to the method (M1) or (M2), where the combustible biomass materials include at least a portion of microwave receptors; and    (3) a method (M3) of processing a biomass fuel compact, comprising heat treating biomass materials of the biomass fuel compact at a base temperature to break oxygen-hydrogen bonds, where the base temperature is below a mean torrefaction temperature of the biomass fuel compact so that torrefaction of a substantial portion of the biomass materials does not occur.
NOVELTY - The system has a water cleanup station (205) including a drawing unit for drawing off hot water vapor from coal (201) and biomass (202) in a kiln (207). A wet scrubber (206) includes a drawing unit for drawing off contaminants and hydrocarbons emanating from pre-processing of the coal and biomass. A steam generator includes a converting unit for converting the vapor from the station to high pressure steam. A chemical looping reactor i.e. gasifier (211), oxidizes the pre-processed coal and biomass from the kiln in conjunction with the steam from the generator and hydrocarbons from the scrubber.    USE - System for pre-processing coal and biomass prior to chemical looping combustion in a burner with air i.e. oxygen, by chemical looping of an oxygen carrier and compression in a diesel engine for industrial applications.    ADVANTAGE - The system removes the vapor and the pollutants to reduce cost and increases efficiency of chemical looping process, while preserving integrity of an oxygen carrier. The system facilitates clean fuels to prevent worldwide air pollution by harmful contaminants inherently present in nearly all carboniferous fuel. The system facilitates efficient combustion process that results in energy production to be cheaper, less polluting and more efficient by removing the vapor and the contaminants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for pre-processing coal and biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of components and interconnections to bring raw coal and biomass into a state essentially free of water vapor and pollutants for efficient combustion, gasification or liquefaction.    Coal (201)    Biomass (202)    Water cleanup station (205)    Wet scrubber (206)    Kiln (207)    Gasifier (211)
NOVELTY - A metal complex comprising transition metal, and N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine (DPA-Bpy) or 6'-((bis(pyridin-2-ylmethyl)amino)methyl)-N,N-dimethyl-2,2'-bipyridin-6-amine (DPA-ABpy), or its salt, solvate or hydrate, is new.    USE - As a catalyst, for producing hydrogen from an aqueous solution (claimed).    ADVANTAGE - The metal complexes are efficient electrocatalysts and efficient photocatalysts for producing H2 from an aqueous solution.    DETAILED DESCRIPTION - A metal complex of formula (M'(G')Y')m(X)n(L')a (I) or its salt, solvate or hydrate, is new.    M'=transition metal;    G'=N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine (DPA-Bpy), 6'-((bis(pyridin-2-ylmethyl)amino)methyl)-N,N-dimethyl-2,2'-bipyridin-6-amine (DPA-ABpy), or its derivative;    Y'=absent, halo or water moiety;    X=anion;    m=number of cations per metal complex;    n=number of anions per metal complex;    L'=absent or a neutral molecule;    a=number of neutral molecules per metal complex.    Provided that: when G' is N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine (DPA-Bpy), then M' is not Ru. INDEPENDENT CLAIMS are included for the following:    (1) a catalyst comprising the metal complex (I); and    (2) producing hydrogen from an aqueous solution involving adding the catalyst to the aqueous solution.
NOVELTY - A waste digestate containing 20-70 wt.%. charge having 42-50 wt.% s.m. (sic) containing 35-60 wt.% organic carbon is post-fermented. The organic carbon contained in 10-30 wt.% charge is treated with concentrated sulfuric acid and neutralized with 10-35 wt.% magnesium oxide based on magnesium carbonate with respect to sterilization of microbiological reference conditioning of waste post-fermentation at 108-150 degrees C for 30 minutes and maintaining the temperature of mixture at 2 degrees C/minute or more to obtain mineral-organic fertilizer.    USE - Manufacture of mineral-organic fertilizer (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly manufacture of mineral-organic fertilizer.
NOVELTY - The method involves dispersing (S1) a metal-supported catalyst in which a metal nano-particle is supported by a surface of non-electro conductive material in a solvent dissolved with a polymeric material. The metal supported catalyst dispersed in the solvent is adhered (S2) to a surface of the electro conductive material. The polymeric material is removed (S3) from the metal-supported catalyst adhered to the surface of the electro conductive material.    USE - Method for manufacturing an electrode for a fuel cell.    ADVANTAGE - The method enables making the electro-conductive material to support with the activity of the catalyst and maintain the metal nano-particle in the non-electro-conductive material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrode for fuel cells.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing an electrode for fuel cells.    Step for dispersing a metal-supported catalyst in which metal nano-particle is supported by surface of non-electro conductive material (S1)    Step for adhering metal supported catalyst dispersed in solvent to surface of electro conductive material (S2)    Step for removing polymeric material from metal-supported catalyst (S3)    Solvent removing step (S31)    Step for baking solvent at 200 degree centigrade (S32)
NOVELTY - The system (11) has a temperature detector i.e. thermistor (17), for detecting temperature of hot water in a hot water storage tank (15). A display apparatus displays graduation when the temperature detector detects the temperature more than predetermined temperature. A controller i.e. remote control unit (20), sets a display content of the display apparatus and displays a symbol with shape different from the graduation displayed on the apparatus when a fuel cell unit (12) produces electric power and the temperature detector detects display of temperature less than the former temperature.    USE - Cogeneration fuel cell system.    ADVANTAGE - The hot water storage tank is covered with hot water when the thermistor that detects the temperature of hot water is provided on the hot water storage tank with another thermistor, so that a user can realize that the hot water accumulates, thus eliminating inconvenience in which utilization of hot water is made, and making hot water accumulation to be visible.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a display apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a cogeneration apparatus.'(Drawing includes non-English language text)'    Cogeneration fuel cell system (11)    Fuel cell unit (12)    Hot water storage tank (15)    Thermistor (17)    Remote control unit (20)
NOVELTY - A kind of comprehensive processing method for domestic garbage treatment system, comprising a sewage treatment tank, the sewage treatment tank is divided into separate and sewage pump, drain pipe, the drain pipe pass through a sewage pump, enters into the water collecting tank, and a drain pipe with one end of the water collecting tank is connected with the water storage tank, the other end is a sewage treatment tank is connected with the sewage pipe located in the sewage treatment pool outside of the sewage pump, the sewage pump is located in the sewage pump is connected with the drain pipe of the sewage pump the sewage, the sewage processor is connected with the sewage pipe, purifying and sterilizing tank, a purifying and sterilizing tank is connected with the sewage processor is connected with organic fertilizer fermenting tank, the organic fertilizer fermenting tank is connected with the sewage processor is connected with organic fertilizer granulator, the organic fertilizer granulator connected with the organic fertilizer fermentation tank. Using the system for processing domestic garbage, the domestic garbage into organic fertilizer, which not only reduces the pollution of the domestic waste water and the atmosphere, but also can produce great economic benefit.
NOVELTY - The household appliance has burner that is positioned in the combustion zone. The electrolytic cell is connected with burner. The burner is extended along the electrolytic bath. The fan is provided to guide air to combustion zone through the hydrogen gas flow path.    USE - Household appliance such as cooking appliance (claimed) e.g. indoor grill.    ADVANTAGE - The indoor grill can be maintained in reduced or no ventilation state.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the domestic appliance.    Indoor grill (130)    Grill surface (136)    Cover (138)    Substrate (196)    Cover plate (198)
NOVELTY - A modified silicon dioxide film is modified hydrophobic silica film prepared by doping silane coupling agent through a sol-gel process for five times under 30 KPa, such that the methane is permeated and separated to carbon dioxide.    USE - Modified silicon dioxide film used for separating methane/carbon dioxide.    ADVANTAGE - The film has high hydrophobicity, and gas-separating property.
NOVELTY - Electro-catalysis for producing hydrogen by sodium borohydride solution involves cathode and anode electrodes of electrolytic cell which is sodium borohydride solution with concentration of 0.1-35% is applied to direct current voltage electro-catalysis, catalytically decomposing sodium borohydride solution to generate hydrogen at surface of electrode.    USE - As electro-catalysis method for producing hydrogen (claimed).    ADVANTAGE - The method saves the electric energy, is safe and environment-friendly, and does not generate oxygen.
NOVELTY - A prickly pear leaf valley remain alcohol extraction process involves supercritical fluid extraction technology to extract prickly pear leaves sitosterol.    USE - As prickly pear leaf valley remain alcohol extraction process (claimed).    ADVANTAGE - The method has simple technique and no pollution, and it can effectively extract sitosterol.
NOVELTY - Method for producing trees and flowers special fertilizer involves (a) adding 5% whitewash in 1000 kg fresh vinegar residues to adjust pH to 6.8-7.6, (b) adding 0.3% baiyibao EM stock solution and 0.2% corruption agent to 1000 kg fresh vinegar residues, transporting the stirred vinegar residues in a fermentation tank, and conducting anaerobic digestion at the temperature of 35 degrees C for 35 days, and (c) collecting sewage gas produced by fermentation in an air storage tank, and separating surplus biogas residues and biogas slurry to obtain trees and flowers special liquid fertilizer.    USE - The method is useful for producing trees and flowers special fertilizer.    ADVANTAGE - The method effectively uses vinegar residues to produce the trees and flowers special fertilizer, saves resources, recycles waste product produced by the method, reduces environmental pollution, improves recycling and harmless of the vinegar residues, and increases peasant income through produced special fertilizer. The fertilizer achieves high yield and high quality in agricultural prospective and is suitable for industrial application.
NOVELTY - This utility model claims a fully sealed production azamethiphos, as a reaction device, comprising a first reaction unit, a second reaction unit and a third reaction unit. The first reaction unit comprises a rotary storage kettle, a oxazole (4, 5-b) -2 (3H)-ketone material storing tank, a N, N-dimethyl formamide storage tank, a poly-formaldehyde material storage tank and a sulfoxide chloride storage tank. The first reaction unit comprises a first inlet and a first outlet a first powder-liquid mixing pump, the first powder-liquid mixing pump. The oxazole (4, 5-b) -2 (3H)-ketone material storing tank, N, N-dimethyl formamide storage tank and poly-formaldehyde material storage tank is connected with the first inlet, the first outlet is connected with the rotational flow. The rotary storage kettle comprises a first main body, the first main body is hollow to form a first reaction chamber, the first reaction chamber is an inverted conical structure. This utility model claims a reaction device, to a radically avoids harmful gas leakage, which is good for environment protection.
NOVELTY - An oleaginous microorganism suitable for production of renewable materials comprises a genetic modification not present in an unmodified microorganism, and where the modified microorganism produces a fermentation broth having a lower viscosity than a fermentation broth produced by the unmodified microorganism when grown in culture, is new.    USE - The microorganism is useful for producing renewable materials, preferably for producing a biofuel precursor and biofuel. The biofuel is used for powering a vehicle (all claimed).    ADVANTAGE - In addition to reduced exocellular polysaccharide formation, dry morphology mutants of multiple strains show reduced viscosity, improved oxygen mass transfer, improved fatty acid fermentation yield on carbon, and high mass transfer coefficient to support high cell density levels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a fermentation broth produced by the modified microorganism above;    (2) a method of producing a biofuel precursor by culturing the microorganism above and collecting the fermentation broth produced by the microorganism;    (3) a method of producing a biofuel by (a) supplying a carbon source, (b) converting the carbon source to fatty acids within the microorganism above, (c) culturing the microorganism to a cell density of at least 50 grams cellular dry weight per liter in a fermentation broth having a viscosity of less than 1100 centipoise (cP), (d) extracting fatty acids from the microorganism, and (e) reacting the fatty acids to produce a biofuel;    (4) a biofuel produced by the method of (3); and    (5) a method of powering a vehicle by combusting the biofuel of (4) in an internal combustion engine.
NOVELTY - A recombinant Escherichia coli cell comprises nucleic acid sequences that encode phosphatidic acid phosphatase (PGP) and diacylglycerol acyltransferase (DGAT), where upon expression of the PGP and DGAT, the cell produces triglyceride having 16C acyl chain.    USE - For producing triglycerides (claimed), used as raw material for producing biodiesel and component of household products e.g. lotions, lubricants and cooking oils; for producing compounds on commercial scale e.g. therapeutic proteins and small molecules in pharmaceutical industry and chemicals e.g. ethanol for biofuel industry.    ADVANTAGE - The production of triglycerides in recombinant E. coli cell is efficient for producing at least 2 (preferably at least 5) g/l glucose, having 18C or 14C or at least two 16C acyl chains. The E. coli expressing PGP and DGAT can also express phasin, where phasin is lipid binding protein that can coat lipid droplets to protect them from degradation and can act as point of seeding for triglyceride formation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing triglycerides involving providing recombinant Escherichia coli cell that expresses PGP and DGAT; culturing the cell in media to produce triglycerides; and isolating the triglycerides from the media.
NOVELTY - Power station-based methanation system (1) comprises a fossil fuel-fired power station (2) with an electrolysis unit (3), and a methanation reactor (4). The power station and the electrolysis unit are designed to supply the methanation reactor with starting materials for a methanation reaction, and the electrolysis unit is operated in a charging state and a discharging state, where an electric power is supplied to the electrolysis unit and a chemical energy store is charged at the same time, during the charging state and the chemical energy store is discharged during the discharging state.    USE - Used as a power station-based methanation system.    ADVANTAGE - The power station-based methanation system: ensures a continuous production of synthetic methane; and enables an increased demand of electrical energy into the public power supply network.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for operating the methanation system, comprising either: supplying water to the electrolysis unit, electrolytically or chemically converting the water into hydrogen, mixing hydrogen with the carbon dioxide obtained from power station, and supplying the mixture of hydrogen and carbon dioxide as starting materials to the methanation reactor; or supplying a mixture of water and carbon dioxide obtained from the power plant, electrolytically or chemically converting mixture of water and carbon dioxide into hydrogen and carbon monoxide, and supplying the mixture of hydrogen with carbon monoxide as starting materials to the methanation reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methanation system.    Methanation system (1)    Fossil fuel-fired power station (2)    Electrolysis unit (3)    Methanation reactor (4)    Supply line (11)
NOVELTY - Device (100) for producing regenerative methanol based on carbon dioxide containing methane gas, comprises: a carbon dioxide reformer, which is fed with the carbon dioxide-containing methane gas, and which has an output region, in which a first synthesis gas is provided; and a first methanol synthesis reactor, which is fed with a feed gas, which corresponds to the first synthesis gas, or which is derived from the first synthesis gas, where the methanol synthesis reactor is adapted to exothermic catalytic synthesis of regenerative methanol.    USE - The device is useful for producing regenerative methanol based on carbon dioxide containing methane gas.    ADVANTAGE - The device ensures an enhanced yield of methanol, and ensures an inexpensive method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a process for providing regenerative methanol (Drawing includes non-English language text).    Device (100)    Gas supply (101)    Controller (110)    Storage (111)    Hydrogen gas supply (120)
NOVELTY - Biomass energy production using biological waste combination, involves: using production engineering bacterium Clostridium acetobutylicum strain fermentation substrate of biological waste comprising food waste, agricultural waste, and mycelium waste produced during the production of antibiotics, where fermentation substrate combination includes the wastes in different proportions, and the production engineering bacteria strain is a fusiform-shaped bacillus, where the biomass energy product contains acetone, ethanol, butanol and isopropanol.    USE - For biomass energy production using biological waste combination (claimed).    ADVANTAGE - The method for production of biomass energy, not only makes full use of the original bio-waste, which can pollute the environment, but also produces biomass energy and purifies environment; maximizes the recycling; improves the efficiency of the fermentation and speed of cell growth and obviously shortens fermentation time, which greatly reduces the fermentation cost.
NOVELTY - The hydrolyzing apparatus has casing with which electrolyte solution is filled. The inside of casing is separated into an oxygen generation chamber (21) and hydrogen producing chamber (31) by electrolytic membrane (70). A light-receiving window is provided with the electrode layer used as working electrode (50). An optical semiconductor catalyst layer is laminated in electrode layer. A counter electrode (60) is positioned at hydrogen producing chamber and equipped with base fixed to casing. A porous portion (63) is held in the base to transmit the electrolyte solution.    USE - Hydrolyzing apparatus for use in tandem-type sunlight utilization apparatus (claimed).    ADVANTAGE - Since the porous portion is held in the base to transmit the electrolyte solution, the fresh electrolyte solution always contact counter electrode. Thus the decomposition reaction of water is stimulated which is sufficient for utilization. As light-receiving window, porous portion, and light transmissive window are located in straight line, the light of the component which is not absorbed by the optical semiconductor catalyst in the light taken in from the light-receiving window is released from light transmissive window, without receiving damping by the irregular reflection in casing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a tandem-type sunlight utilization apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrolyzing apparatus. (Drawing includes non-English language text)    Oxygen generation chamber (21)    Hydrogen producing chamber (31)    Working electrode (50)    Counter electrode (60)    Porous portion (63)    Electrolyte membrane (70)
NOVELTY - The apparatus has vertical waste material gasified melting furnace (1) which melts thermal decomposition residue of waste material. One of secondary combustion chamber (10) and boiler (12) is connected to carbide material manufacturing apparatus (13), so that the waste heat is supplied as heat source. The carbide manufacturing apparatus is connected to waste material gasified melting furnace, so that the carbide produced by carbide manufacturing apparatus is supplied to waste material gasified melting furnace as fuel.    USE - Waste material gasification fusion apparatus for fusion of decomposition residue of thrown-in waste material such as municipal solid waste, shredder dust, wood type biomass such as wood land surplus material, coppiced timber, unused tree, lumber surplus material, construction waste, rice straw, and chaff, and unused biomass resource such as paper manufacture type biomass, agricultural residue, livestock excrement, and foodstuff waste material.    ADVANTAGE - As the carbide produced by carbide manufacturing apparatus is supplied to waste material gasified melting furnace as fuel by connecting the carbide manufacturing apparatus to gasified melting furnace, the heat energy of biomass feedstock is used effectively, and the amount of coal coke is reduced, so that the discharge amount of carbon dioxide is reduced, and the operating cost of waste material gasified melting furnace is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste material gasification fusion apparatus. (Drawing includes non-English language text)    Waste material gasified melting furnace (1)    Gas exhaust port (3)    Secondary combustion chamber (10)    Boiler (12)    Carbide manufacturing apparatus (13)
NOVELTY - Preparation of benzimidazole involves using 2-haloanilines, dihalomethane and sodium azide in the present of copper salt as the catalyst, nitrogen donating bidentate ligand, and dimethyl sulfoxide as a solvent at 100-150 degrees C for 12-36 hours reaction time.    USE - For preparation of benzimidazole (claimed), used in various fields such as pharmaceutical, and fine chemicals.    ADVANTAGE - This method gives 50-80% yield of corresponding benzimidazole molecules with different carbon sources; and is economically cheaper and safer as compared to prior art method.
NOVELTY - Making Diminazene diaceturate (I) involves a) converting p-nitro benzamide into p-nitro benzonitrile; b) converting optionally in situ, p-nitro benzonitrile into p-nitro benzamidoxime; c) reducing p-nitro benzamidoxime to obtain p-amino benzamidine dihydrochloride; d) diazotizing p-amino benzamidine dihydrochloride, followed by coupling of diazonium salt of p-amino benzamidine dihydrochloride with p-amino benzamidine dihydrochloride in presence of catalytic amount of sulfamic acid to obtain diminazene; and e) reacting obtained diminazene with aceturic acid to form diminazene diaceturate.    USE - In the preparation of Diminazene diaceturate (claimed) which is used in the treatment of trypanosomiasis and babesiosis.    ADVANTAGE - The process provides short reaction time and high production yield; and is a very cost effective and environment friendly process.
NOVELTY - A kind of oil shale drying, heating, oil refining and semi-coke combustion integrated device, wherein it is as follows: crushing the oil shale or 15 mm in a gas indirect heating and drying, burning the hot ash from the circulating fluidized bed combustion furnace with solid heat carrier into the dry distillation reactor to a heat exchange the dry distillation oil-refining from high temperature flue gas of the circulating fluidized bed combustion furnace is sent to high temperature gas indirect dry distillation reactor with oil shale heat exchange to realize dry distillation oil-refining of solid fuel, the solid heat carrier of the dry distillation reactor or a direct heat exchange drying heater shale semi-coke by semi-coke hopper and high temperature gas indirect dry distillation reactor discharge of solid semi-coke is sent into the circulating fluidized bed combustion furnace continuously, at the same time the combustion of the circulating fluidized bed furnace is discharged from the redundant hot ash slag cooling through the cooler into the building material. A finish oil shale fuel drying, heating, oil refining and semi-coke combustion. Also can be used for coal, oil sand, waste tyre, petroleum coke, organic waste and biomass.
NOVELTY - A prochloraz-containing composition is a microcapsule suspending agent-water emulsion formed by mixing prochloraz microcapsule suspending agent and prochloraz water emulsion and comprises 1-60 %mass prochloraz, 1-25 %mass solvent, 1-20 %mass encapsulating agent, 1-10 %mass surfactant, 0.5-10 %mass antifreezing agent, 0.01-3 %mass thickener, 0-5 %mass pH regulator, 0.01-1 %mass defoaming agent, 0.01-1 %mass preservative and remainder of water.    USE - Prochloraz-containing composition is useful for preventing and/or treating fungal disease in agricultural field, where the fungal disease includes rice blast, wheat scab and bakanae disease.    ADVANTAGE - The invention also provides application of the new preparation formulation containing prochloraz in the field of agricultural fungus disease control. The preparation lowers the consumption of organic solvent, reduces the harm to the environment, has favorable fast-acting property and long-acting property, and is stable in performance and convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of prochloraz-containing composition, which involves mixing and processing raw material components.
NOVELTY - A granular preparation comprises 0.01-10 mass% chlorfenapyr, cartap hydrochloride, and an agrochemical auxiliary agent. The weight ratio of chlorfenapyr and cartap hydrochloride is 1:1-1:50.    USE - A granular preparation used for preventing and controlling paddy rice pests (claimed).    ADVANTAGE - The granular preparation is safe, environment-friendly, and achieves long pesticide effect lasting period.
NOVELTY - The method involves performing an emulsification process by an emulsifying agent. Heavy oil is heated at 40 degrees centigrade to 60 degrees centigrade under the stirring condition. Biomass oil is added with the emulsifying agent under the stirring state. A single series catalytic hydrocracking process is performed for refining process for heavy component.    USE - Method for mixing a heavy component in biomass oil with heavy oil e.g. vacuum gas oil, residual oil, deasphalted oil, coking wax oil, decompressed wax oil, and straight-run diesel oil (all claimed), obtained by secondary processing of petroleum oil.    ADVANTAGE - The method enables providing better energy density, good fluidity, and stability, and reducing the oxygen content and viscosity, thus enhancing the practicability of the biomass oil in a cost effective manner.
NOVELTY - Wugang wood or Qinggang wood is dried, closed-evaporated, carbonized, smelted and cooled in a carbonization kiln, to obtain white charcoal.    USE - Production of white charcoal (claimed).    ADVANTAGE - The method provides white charcoal having excellent strength, crack resistance and metallic luster, density of 1.05-1.10 g/cm3 or less, hardness of 5.6-5.8, heating value of 8800 kilocalories or less, smooth surface, and low breaking characteristics.
NOVELTY - Preparing roflumilast, comprises treating 3-cyclopropylmethoxy-4-difluoromethoxy benzoic acid with carbonyldiimidazole in a first organic solvent at room temperature, followed by concentration of the reaction mixture and reaction of the resulting compound with 4-amino-3,5-dichloropyridine in a second organic solvent and in presence of a base at reflux temperature to give roflumilast.    USE - The process is useful for preparing roflumilast (claimed), which is useful for treating inflammatory conditions such as asthma and chronic obstructive pulmonary disease. No biological data given.    ADVANTAGE - The process provides roflumilast with good yield and purity in an economical and environmentally friendly manner.
NOVELTY - A process of preparation of bicalutamide involves: oxidation of 4-cyano-3-trifluoromethyl-N-(3-p-fluorophenylsulfanyl-2-hydroxy-2-methylpropionyl) aniline with m-chloroperbenzoic acid (mCPBA) in an organic solvent; followed by adding ketonic solvent, washing with solution of sodium sulfite and sodium carbonate, and isolating the product with combination of organic solvent and anti solvent.    USE - In the preparation of bicalutamide (claimed).    ADVANTAGE - The process avoids the use of large excess of halogenated solvents as used in the prior art methods; eliminates the presence of undesired by products in the final product during the isolation of bicalutamide; does not require any column chromatography for purification; provides bicalutamide having purity more than 99.5%; and is effective, environmentally friendly and easily implemented in industrial scale.
NOVELTY - Preparing decitabine comprises treating 4-amino-1H-(1,3,5)triazin-2-one compound (II) with a base comprising alkali-metal carbonate or alkali earth metal carbonate, adjusting the pH of reaction mixture, and isolating decitabine.    USE - The process is useful for preparing decitabine (claimed), which is useful for treating myelopathic syndrome. No biological data given.    ADVANTAGE - The process simply and safely prepares decitabine under optimal basic condition, without causing degradation of decitabine, with high yield and enantiomeric purity of 99.8% in an economical and an environmental friendly manner.    DETAILED DESCRIPTION - Preparing decitabine comprises treating 4-amino-1H-(1,3,5)triazin-2-one compound of formula (II) with a base comprising alkali-metal carbonate or alkali earth metal carbonate, adjusting the pH of reaction mixture, and isolating decitabine.    R = protecting group, preferably aryl or acyl protecting group such as toluolyl or acetyl.    An INDEPENDENT CLAIM is included for purifying decitabine comprising (a) providing a solution of decitabine in a first solvent, (b) substantially distilling off the solvent of step (a), (c) adding second solvent, and (d) isolating pure decitabine.
NOVELTY - An organic fertilizer is manufactured by mixing straw, agricultural processing residues, livestock manure and biological agents at ratio of 1:1:1:1, adding 10-15 wt.% water, granulating into 80-100 mesh particle size, fermenting at 50-60 degrees C for 24-30 hours, granulating at particle size classification including 1-3 mm, 4-6 mm and 6-9 mm, drying to controlled moisture content of not greater than 10% and packaging.    USE - Method for manufacturing organic fertilizer (claimed).    ADVANTAGE - The method is simple and easy to operate.
NOVELTY - An organic fertilizer is prepared by carrying out raw material pretreatment by piling up fresh cow dung in fermentation pool, stacking, turning over, adding oil cake, microbial agents and water, mixing, fermenting, turning over, stacking and composting, adding humic acid, decomposing, mixing, stacking at controlled temperature, turning over, sieving, drying and packing.    USE - Method for preparing organic fertilizer for tobacco (claimed).    ADVANTAGE - The fertilizer has high organic matter content which promotes formation of soil structure, improves soil physical properties and quality of tobacco with reduced diseases.    DETAILED DESCRIPTION - An organic fertilizer is prepared by:    (A) carrying out raw material pretreatment by piling up 200-300 g/ton fresh cow dung in fermentation pool, stacking, raising temperature to 50 degrees C, turning over every 4-5 days for 1-2 times, controlling temperature at not greater than 60 degrees C, stacking for 12-15 days and fermenting;    (B) adding 200-300 g/ton oil cake, microbial agents and water, mixing, fermenting at 40 degrees C, turning over every 4-5 days for 2-3 times, controlling temperature at not greater than 50 degrees C, stacking for 12-15 days and composting; and    (C) adding 10-30 wt.% humic acid, decomposing, mixing, stacking at controlled temperature of not greater than 40 degrees C, turning over every 2-3 days for 1-2 times, sieving, drying and packing.
NOVELTY - The device has a methane storage tank (T5) connected to a marsh gas steel bottle (T6). A rotating packed bed reactor (T7) is connected to a liquid storage tank (T4). The methane storage tank and a motor (T8) are connected to a purifying gas storage tank (T1) with a gas exhaust opening (G1). A stock solution storage tank (T2) is provided with an opening (G2). A regeneration tank (T3) is provided with a feeding port (G3). The liquid storage tank is provided with a cleaning liquid mouth (G4). The methane storage tank is provided with a marsh gas exhaust opening (G5).    USE - Methane separation and purification device.    ADVANTAGE - The methane separation and purification device has wide source, low cost and is environmental-friendly due to the selected absorbing agent. The device includes simple reaction process, moderate reaction condition, convenience for operation, high carbon-dioxide absorption rate and high purity of the separated methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of methane separation and purification device for purifying methane by absorbing carbon-dioxide through alkaline process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane separation and purification device.    Gas exhaust opening (G1)    Opening of stock solution storage tank (G2)    Feeding port (G3)    Cleaning liquid mouth (G4)    Marsh gas exhaust opening (G5)    Purifying gas storage tank (T1)    Stock solution storage tank (T2)    Regeneration tank (T3)    Liquid storage tank (T4)    Methane storage tank (T5)    Marsh gas steel bottle (T6)    Rotating packed bed reactor (T7)    Motor (T8)
NOVELTY - Preparation of nano-porous iron-base oxygen carrier used for biofuel involves mixing ferric nitrate and aluminum nitrate as precursors, citric acid as a complexing agent and polyethyleneglycol as a pore-foaming agent and dispersing agent to prepare a aqueous solution, stirring uniformly to obtain a sol, evaporating the sol to bubbling state to obtain a gel, drying the gel, and calcining.    USE - Preparation of nano-porous iron-base oxygen carrier used for biofuel (claimed).    ADVANTAGE - The environmentally-friendly nano-porous iron-base oxygen carrier is manufactured efficiently and economically with excellent reaction activity and stability, by simple.
NOVELTY - This utility model relates to polyol purifying device technology field, it is a kind of frostbite prevention and dehydration of natural gas by alcohol purification device, comprising a conveying pump, a first filter device, hydrocarbon removing de-waxing device, decolouring and removing high molecular weight oxide, anion exchange, cation exchange device and the second filter device, the liquid outlet of the conveying pump through a pipe connected with the liquid inlet end of the first filter device communicated with the lower part of the first filter device on the upper part of the liquid outlet through a pipe and the liquid inlet of the hydrocarbon de-waxing device communicated with the lower part, the liquid outlet of the hydrocarbon de-waxing device on the upper part through a pipe and the liquid inlet of the decolouring and removing high molecular weight oxide lower part are connected with each other. This utility model has reasonable structure and convenient use, the frostbite prevention and dehydration of natural gas to be purified with polyol, the frostbite prevention and dehydration of natural gas can be repeatedly used, which avoids the waste discharge polyol caused by environment pollution, and it saves raw material cost of a polyol.
NOVELTY - A low freezing point motor fuel from biological oil producing method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing two hydrogenation reactors. The hydrogen-rich gas is recycled at the first stage, and the liquid is entered to a modification reaction zone. The sub-hydrogen gas of stream is recycled at the second stage. The liquid product is subjected to fractionation. Active components of the hydrogenation catalyst at the first stage are materials selected from reduction state of tungsten, molybdenum, nickel and cobalt.    USE - Method for producing low freezing point motor fuel from biological oil.    ADVANTAGE - The method enables producing fuel with better activity stability of the catalyst and stable and long period device.    DETAILED DESCRIPTION - A low freezing point motor fuel from biological oil producing method using two-stage hydrogenation method involves passing biological oil raw material and hydrogen through a first stage hydrogenation reaction zone containing two hydrogenation reactors, where the mixture is passed through a low temperature operation reactor, and through a high temperature operation reactor. The hydrogen-rich gas is recycled at the first stage, and the liquid is entered to a second stage hydrogenation modification reaction zone. The sub-hydrogen gas of the stream generated from hydrogenation modification is recycled at the second stage. The liquid product is subjected to fractionation to obtain naphtha and low freezing point diesel oil. Active components of the hydrogenation catalyst at the first stage are materials selected from reduction state of tungsten, molybdenum, nickel and cobalt, and active components of the hydrogenation catalyst at the second stage are materials selected from sulfurization state of tungsten, molybdenum, nickel and cobalt.
NOVELTY - The system has an electric arc chamber in which carbonaceous material (1) and carrier gas are provided from a material inlet and hollow channel through a conveying channel. The conveying channel is connected with a chilling medium inlet of reaction product for chilling anode of a reaction tube (14). The working gas (4) is flowed through electric arc chamber between the hollow cathode (11) and anode to generate plasma gas by mixing with the carbonaceous material and carrier gas at maximum temperature zone of the chamber.    USE - Plasma cracking carbonaceous material reactor system used for producing acetylene.    ADVANTAGE - The thermal efficiency and cracking product yield can be improved effectively. The gaseous and liquid feeding material can be processed easily, hence loss can be reduced. The protecting wall can be secured. The high concentration or a large amount of volatile can be released, hence straw fast thermal-cracking product can be improved. The consumption of superfine carbon monoxide by selecting grain size distribution of carbonaceous materials can be reduced. The low grade and oxygen content carbonaceous material can be utilized.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the plasma cracking carbonaceous material reactor system.    Carbonaceous material (1)    Working gas (4)    Hollow cathode (11)    Side wall (13)    Reaction tube (14)
NOVELTY - An environmentally-friendly energy-saving methanol gasoline comprises methanol, naphtha and an additive which is a compound additive containing 6-15 wt.% turpentine, 4-13 wt.% L-menthol, 5-19 wt.% camphor, 11-29 wt.% borneol, 5-25 wt.% borneol flakes, 16-39 wt.% isobutene, 11-32 wt.% monoethyl amine and 3-4 wt.% 2 6-di-tert-butyl-para-cresol.    USE - Environmentally-friendly energy-saving methanol gasoline is used for gasoline engine.    ADVANTAGE - The methanol gasoline is environmentally-friendly and energy-saving.
NOVELTY - A hydrogen sulfide removal reagent comprises 40-50 wt.% formaldehyde, 5-10 wt.% acetaldehyde, 4-8 wt.% acetone and remainder of purified water.    USE - Hydrogen sulfide removal reagent is used for desulfurization of biogas.    ADVANTAGE - The reagent has high hydrogen sulfide-removal effect.
NOVELTY - Continuous synthesis of biodiesel by a microreactor involves dissolving predetermined amount of an alkaline catalyst in lower alcohol, respectively injecting the solution and grease into a continuously heated microreactor, reacting at 40-64 degrees C, and controlling retention duration of the materials in the microreactor for 0.1-1 minute. The micro passage of the microreactor comprises a micro mixing passage and a micro reaction main passage.    USE - Continuous synthesis of biodiesel by microreactor (claimed).    ADVANTAGE - The additional pre-mixing of the reaction materials is not required. The microreactor integrates functions of mixing and reacting, and operates under normal pressure, and has improved mixing efficiency and reaction efficiency. The retention duration is further shortened, and production intensity is improved.
NOVELTY - Wastewater treatment system, preferably microbial fuel cell wastewater treatment system, has anode and cathode, where the anode is without any modification, cathode camber of the microbial fuel cell is inoculated with nitrated sludge, and cathode camber of the microbial fuel cell is added and embedded with aerobic denitrifying bacteria particles, to play effects of nitrification and denitrification in one reaction zone synergistically, fully utilize DO and residual carbon sources of the cathode, and realize purposes of denitrification and further chemical oxygen demand (COD) removal.    USE - The wastewater treatment system, preferably microbial fuel cell wastewater treatment system is useful for improving nitrogen removal effect (claimed).    ADVANTAGE - The wastewater treatment system is low in energy consumption, stable, and free of waste sludge, and has continuous and stable voltage output.    DETAILED DESCRIPTION - Wastewater treatment system, preferably microbial fuel cell wastewater treatment system, has anode and cathode, where the anode is without any modification, cathode camber of the microbial fuel cell is inoculated with nitrated sludge, and cathode camber of the microbial fuel cell is added and embedded with aerobic denitrifying bacteria particles, to play effects of nitrification and denitrification in one reaction zone synergistically, fully utilize DO and residual carbon sources of the cathode, and realize purposes of denitrification and further chemical oxygen demand (COD) removal.
NOVELTY - Catalytic synthesis of propyl caffeate comprises subjecting caffeic acid and propanol at mol ratio of (1:5)-(1:100) into direct chemical reaction at 40-80 degrees C for 12-21 hours under catalytic effect of p-toluenesulfonic acid, which is added at 15 mass% of total mass of reactants.    USE - Catalytic synthesis of propyl caffeate.    ADVANTAGE - The method has mild reaction condition, environment friendly, overcomes disadvantages of existing complex operation that produces several by-products, and provides propyl caffeate at high yield.
NOVELTY - Synthesis of sulfamoyl carbamate compound comprises reacting 2-sulfamoyl-N,N-dimethyl-nicotinamide and dimethyl carbonate at 20-40 degrees C for 4-6 hours under the action of sodium methoxide catalyst, zinc acetate or ytterbium trifluoromethanesulfonate, neutralizing using concentrated hydrochloric acid, filtering to remove sodium chloride, drying filtrate by anhydrous sodium sulfate and evaporating solvent.    USE - Method for synthesizing sulfamoyl carbamate compound (claimed).    ADVANTAGE - The method avoids using highly-toxic chloroformate and reduces waste discharge.
NOVELTY - A naphtha industrial cracking furnace value maximization model construction method involves establishing a model based on naphtha steam cracking experiment, collecting normal pentane yield data, checking model calculation result in accordance with actual operation data, and calculating cracking product or petrochemical product value of the cracking furnace.    USE - Method for constructing naphtha industrial cracking furnace value maximization model.
NOVELTY - A naphtha industrial cracking furnace value maximization model constructing method involves establishing a model based on naphtha steam cracking experiment using mathematical modeling method for making industrial cracking depth of industrial ethylene cracking furnace product yield prediction model, calculating yield of product cracking naphtha according to physical property of industrial cracking furnace operation condition, collecting pentane yield data, checking normal pentane yield and establishing naphtha cracking depth of industrial ethylene cracking furnace product value maximum model.    USE - Method for constructing naphtha industrial cracking furnace value maximization model.
NOVELTY - A clean fuel contains 5-99 vol.% methanol, 0.5-3.5 vol.% ethanol, 0.2-1.5 vol.% additive, and 0-94 vol.% gasoline.    USE - Clean fuel for vehicle (claimed).    ADVANTAGE - Clean fuel reduces gas emission and has good product quality. Production process is safe, simple, and easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of clean fuel which involves loading ethanol, adding additive, stirring to mix uniformly, adding raw materials at normal temperature and pressure, stirring, standing for 15-20 minutes, and preparing finished product.
NOVELTY - An alcohol-based fuel oil contains 57.5-67.5 wt.% fuel oil, 10-20 wt.% fatty acid, 10-20 wt.% crude methanol, 0.5-1.5 wt.% diethanolamine, and 0.1-1 wt.% ethyl nitrate.    USE - An alcohol-based fuel oil (claimed).    ADVANTAGE - Alcohol-based fuel oil has high stability, and preparation process is simple and has high utilization rate of waste oil as raw material and low production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol-based fuel oil which involves mixing fuel oil, fatty acid, diethanolamine, and ethyl nitrate, heating to 40 degrees C, adding crude methanol, and using high speed shearing and stirring to form clear and transparent liquid.
NOVELTY - A composite methanol gasoline is prepared by mixing castor oil and biodiesel, adding mixture to methanol to obtain 1st solution, adding 0.5-5 vol.% sodium carbonate, 0.5-5 vol.% dimethyl ether, and 0.01-0.5 vol.% propiolic alcohol to 1st solution to obtain 2nd solution, stirring, and mixing 2nd solution and 85-97# gasoline.    USE - Preparation of composite methanol gasoline (claimed).    ADVANTAGE - Preparation process reduces production cost and is environment-friendly.    DETAILED DESCRIPTION - A composite methanol gasoline is prepared by mixing castor oil and biodiesel, adding mixture to methanol to obtain 1st solution, adding 0.5-5 vol.% sodium carbonate, 0.5-5 vol.% dimethyl ether, and 0.01-0.5 vol.% propiolic alcohol to 1st solution to obtain 2nd solution, stirring, and mixing 2nd solution and 85-97# gasoline, in which volume ratio castor oil:biodiesel:mixture is 1:1-10:1, biodiesel is commercial industrial grade product prepared from castor oil, methanol is commercially available industrial grade product, volume ratio mixture:methanol is 1:1-10, calcium carbonate, dimethyl ether, and propiolic alcohol are industrial grade products with /-90% purity, and volume ratio 2nd solution:gasoline is 15-85:85-15.
NOVELTY - Biomass lubricating oil is prepared by flash dehydrating kitchen waste edible grease, removing impurities, performing esterification in acid catalyst at 65-75 degrees C for 2-4 hours by adding methanol, recycling excess methanol, removing acid catalyst and produced water until acid value is less than or equal to 2 mg KOH/g, performing transesterification in base catalyst at 65-75 degrees C for 0.5-1 hours, recycling excess methanol, separating to obtain crude glycerol ester, distilling crude ester to obtain refined methyl ester, mixing methyl ester:hydrogen peroxide:formic acid with weight ratio of 100:30-50:5-15, and heating.    USE - Preparation of biomass lubricating oil for trucks (claimed).    ADVANTAGE - Biomass lubricating oil improves oxidation stability and is highly biodegradable, and preparation process is simple, environment-friendly, and low-cost.    DETAILED DESCRIPTION - Biomass lubricating oil is prepared by flash dehydrating kitchen waste edible grease, removing impurities, performing esterification in acid catalyst at 65-75 degrees C for 2-4 hours by adding methanol, recycling excess methanol, removing acid catalyst and produced water until acid value is less than or equal to 2 mg KOH/g, performing transesterification in base catalyst at 65-75 degrees C for 0.5-1 hours, recycling excess methanol, separating to obtain crude glycerol ester, distilling crude ester to obtain refined methyl ester, mixing methyl ester:hydrogen peroxide:formic acid with weight ratio of 100:30-50:5-15, heating to 40 degrees C, slowly adding hydrogen peroxide dropwise at uniform dropping rate for 2-3 hours, controlling temperature at 55-60 degrees C until addition of hydrogen peroxide is complete, controlling reaction temperature at 60 degrees C, insulating for 6-8 hours to obtain epoxidized fatty acid methyl ester, and adding extreme pressure anti-wear additive and pour point depressant.
NOVELTY - Microbial inoculum for production of fertilizers, contains actinomycetes, yeast, Bacillus, Lactobacillus and photosynthetic bacteria, actinomycetes which is preferably halophilic actinomycetes, multi-spore actinomycetes (Actinopolyspora halophila), the yeast is Saccharomyces cerevisiae, Bacillus is Bacillus subtilis spore, Lactobacillus is Lactobacillus acidophilus, and the photosynthetic bacteria is Rhodobacter sphaeroides.    USE - The microbial inoculum and the process are useful for the production of fertilizers, preferably earthworm bacterial fertilizer (claimed).    ADVANTAGE - The production technique can be used for producing fertilizers, especially an earthworm bacterial fertilizer produced in cooperation with earthworms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an earthworm fertilizer, prepared by: (1) mixing plant fiber, animal manure and earthworms, such earthworm breeding for 1-10 months, preferably 2-6 months; (2) adding water to improve the resulting moisture content of the treated product earthworm (preferably increased to 55-65% (w/w)), and mixing the bacterium; and (3) reacting the product from step (2), keeping the temperature to 45-70 degrees C for 5-30 days fermentation, preferably keeping the temperature at 50-65 degrees C to ferment for 8-20 days.
NOVELTY - A hydrogen deoxidation catalyst comprises metal component as active component supported on a carrier. The active component comprises main active component and auxiliary active component at mole ratio of 1:0.01-1, and the active component is present at 0.1-15 wt.% of the weight of the carrier.    USE - Hydrogen deoxidation catalyst used in preparing high purity hydrogen (claimed).    ADVANTAGE - The catalyst utilizes easy to obtain raw materials, has simple preparation method and low cost, and is safe to transport and store. The hydrogen purification has low operation temperature and gas pressure. The obtained hydrogen gas has purity of 99.99995%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of the catalyst, comprising adding precursor of active component into a dipping solution, then soaking carrier into the dipping solution for 1-48 hours, drying the carrier at 100-150 degrees C for 6-10 hours, then calcining at 300-800 degrees C for 4-6 hours, and introducing hydrogen to activate for 10-16 hours at 300-500 degrees C to obtain the catalyst; and    (2) hydrogen deoxidation by catalyzing and deoxidizing hydrogen at 100-200 degrees C and 2 MPa to prepare high purity hydrogen.
NOVELTY - Preparation of completely-methanated catalyst involves mixing precursor of active component, auxiliary agent (a) and auxiliary agent (b), dissolving into water to prepare solution (A), adding a precipitating agent into water to form solution (B), adding precursor of carrier into water to prepare solution (C), adding solution (A) into solution (B), precipitating to obtain precipitating system (A1), adding solution (B') into the solution (C), precipitating to obtain precipitating system (B1), and mixing the precipitating system (A1) with precipitating system (B1).    USE - Preparation of catalyst used for high-temperature/low-temperature completely-methanated reaction process for synthesizing natural gas (claimed).    ADVANTAGE - The catalyst has excellent activity, high safety.    DETAILED DESCRIPTION - Preparation of completely-methanated catalyst involves mixing precursor of active component, auxiliary agent (a) and auxiliary agent (b), dissolving into water to prepare solution (A), adding a precipitating agent into water to for solution (B) and solution (B'), adding precursor of carrier into the water to prepare solution (C) or solution (C'), adding the solution (A) into solution (B), precipitating to obtain precipitating system (A1), adding solution (B') into the solution (C), precipitating to obtain precipitating system (B1) or adding acidic solution into the solution (B1') to obtain precipitating system (B1), mixing the precipitating system (A1) with precipitating system (B1). The precursor of carrier is alumina. The auxiliary agent (a) and auxiliary agent (b) are lanthanum oxide, cerium oxide, praseodymium oxide and/or samarium oxide. The precursor of active component contains ferric oxide, titania, chromium oxide, cobalt oxide, copper oxide, zinc oxide, molybdenum oxide, zirconium oxide, magnesium oxide, calcium oxide, strontium oxide and barium oxide.
NOVELTY - A refrigerant comprises 0.51-2.5 %mass tetrahydrothiophene, 8 %mass or less pentafluoroethane and remainder of propane.    USE - Refrigerant for air-conditioning device (claimed).    ADVANTAGE - The refrigerant is environmentally-friendly, and is prepared without using special equipment. The refrigerant does not damage the ozone layer, and has low greenhouse effect index. The user can perceive leakage occurring in air conditioning device containing the refrigerant instantly, and safety is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for air-conditioning device having a detector and a control portion.
NOVELTY - A refrigerant comprises 0.51-2.5 wt.% tetrahydrothiophene, and remaining propane (R290) and 1,1,1,2-tetrafluoroethane (R134a). The content of R290 is higher than that of R134a.    USE - Refrigerant is used in air conditioners (claimed).    ADVANTAGE - The refrigerant is environmentally-friendly (does not damage ozone layer and greenhouse effect index), does not require a special refrigeration device, and can be detected instantly during leakage to ensure user safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for air conditioner using the refrigerant.
NOVELTY - Preparation of biodiesel comprises mixing fat source with 2-100 wt.% free fatty acid content and 1-6C monohydric alcohol in reactor, and separating material to obtain biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method improves reactivity of raw fat, biodiesel yield and purity, and adaptability of raw materials.
NOVELTY - Method for improving soil in saline-alkali land, involves (a) punching the soil to drill holes and improving harden degree of the soil, where the soil comprises sloping lawn and nursery stock, (b) applying fertilizer to improve soil fertility, and (c) watering the soil for penetrating and absorbing fertilizer in the soil.    USE - The method is useful for improving soil in saline-alkali land (claimed).    ADVANTAGE - The method loosen the harden soil and enhances water-holding and fertilizer-retaining capabilities of the soil and improves environmental protection.    DETAILED DESCRIPTION - Method for improving soil in saline-alkali land, involves (a) punching the soil to drill holes and improving harden degree of the soil, where the soil comprises sloping lawn and nursery stock, (b) applying fertilizer to improve soil fertility, where the fertilizer comprises green garbage waste treated microbial organic fertilizer, fine sand and plant growth regulator in volume ratio of 70-80:19-29:1, and the green garbage waste treated microbial organic fertilizer is anaerobic fermentation of organic fertilizer using actinomycetes and Bacillus subtilis, and (c) watering the soil for penetrating and absorbing fertilizer in the soil. An INDEPENDENT CLAIM is included for device for performing the above-cited method.
NOVELTY - Preparing bio-diesel involves: taking raw material oil into glycerol to uniformly mix to form solution A, and then mixing sec-butyl acetate with lipase to form solution B, then mixing solutions A and B in enzyme esterification reactor; filtering esterification reaction to generate gas oil, separating enzyme in crude oil and recycling, centrifugal separating crude lipase and removing slag; and under normal pressure distilling oil to separate excess of butyl and water, and then decompressing and rectifying the biological diesel oil and plant asphalt under 0.002 MPa atmospheric pressure.    USE - For preparing bio-diesel by bio-enzyme (claimed).    ADVANTAGE - The biodiesel prepared by this method has a good kinematic viscosity, high cetane number and a high grease production conversion rate. The method is capable of carrying out the catalytic and recycling; and increases the utilization rate of the enzyme, which effectively reduces the cost.    DETAILED DESCRIPTION - Preparing bio-diesel by bio-enzyme, involves: (1) mixing the raw material: taking raw material oil into glycerol to uniformly mix to form solution A, and then mixing sec-butyl acetate with lipase to form solution B, then mixing the solution A and solution B in the enzyme esterification reactor for further fully esterification reaction and ester exchange reaction; (2) filtering: filtering the esterification reaction using precise filter to generate gas oil, separating the enzyme in the crude oil and recycling, separating crude lipase by centrifugal separation, and removing the slag; and (3) purifying: after the centrifugal separation, under normal pressure distilling oil to separate the excess of butyl and the water generated by the reaction, and then decompressing and rectifying the biological diesel oil and plant asphalt under 0.002 MPa atmospheric pressure.
NOVELTY - A biomass waste resource pyrolysis gasification comprehensive conversion system comprises pyrolysis device (1), air supply device (2), multifunctional heat exchange device (3) and residual heating device. The heat exchange device has outer surface with insulation layer. It has gas channel and condensed water channel, heat exchange device. A gas passage inlet (6) is connected with output pipe of gas-solid separating device (19). A gas passage outlet (7) passes through a guiding device (11) connected to the air supply device.    USE - Biomass waste resource pyrolysis gasification comprehensive conversion system.    ADVANTAGE - The system has biomass waste resource comprehensive transform collecting use rate near 100%.    DETAILED DESCRIPTION - Biomass waste resource pyrolysis gasification comprehensive conversion system comprises pyrolysis device (1), air supply device (2), multifunctional heat exchange device (3) and residual heating device. The heat exchange device has outer surface with insulation layer. It has gas channel and condensed water channel, heat exchange device. A gas passage inlet (6) is connected with output pipe of gas-solid separating device (19). A gas passage outlet (7) passes through a guiding device (11) connected to the air supply device. The heat supply device comprises water storage buffer tank (12), pipeline pump (14), and boiler (15). The multifunctional heat exchange device contains condensate inlet (8) through a control valve.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the biomass waste resource pyrolysis gasification comprehensive conversion system.    Pyrolysis device (1)    Air supply device (2)    Multifunctional heat exchange device (3)    Gas passage inlet (6)    Gas passage outlet (7)    Condensate inlet (8)    Guiding device (11)    Water storage buffer tank (12)    Pipeline pump (14)    Boiler (15)    Gas-solid separating device (19)
NOVELTY - A biomass waste resource pyrolytic carbon gasification comprehensive utilization system comprises conversion air supply device (2), multifunctional heat exchange device (3), residual heating device and pyrolytic device (1). The heat exchange device has gas channel and condensed water channel. A gas passage inlet (6) is connected with the pyrolysis device.    USE - Biomass waste resource pyrolytic carbon gasification comprehensive utilization system.    ADVANTAGE - The system has biomass waste resource conversion rate of 100%.    DETAILED DESCRIPTION - Biomass waste resource pyrolytic carbon gasification comprehensive utilization system comprises conversion air supply device (2), multifunctional heat exchange device (3), residual heating device and pyrolytic device (1). The heat exchange device has gas channel and condensed water channel. A gas passage inlet (6) is connected with the pyrolysis device. The multifunctional heat exchange device has condensed liquid outlet (10) connected with separation device (13). It has heat insulating layer. The residual heating device comprises water storage buffer tank, boiler (15) and heat supply pipe net (16).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the biomass waste resource pyrolytic carbon gasification comprehensive utilization system.    Pyrolytic device (1)    Conversion air supply device (2)    Multifunctional heat exchange device (3)    Gas passage inlet (6)    Condensed liquid outlet (10)    Separation device (13)    Boiler (15)    Heat supply pipe net (16)
NOVELTY - A methanol diesel oil microemulsion is prepared by adding 0.4-0.8 pt. wt. oleic acid into 7-9 pts. wt. diesel oil, stirring to dissolve, adding 0.1-0.3 pt. wt. stearic acid, quickly stirring to obtain solution A, dissolving 0.05-0.2 pt. wt. isooctanol, 0.05-0.2 pt. wt. isobutanol, 0.05-0.3 pt. wt. ethyl acetate and 0.05-0.2 pt. wt. triethanolamine in 1-5 pts. wt. methanol to obtain solution B, quickly stirring solution B into solution A for 60-80 minutes to obtain clear microemulsion, adding 0.001-0.2 pt. wt. combustion promoter and quickly stirring to completely dissolve.    USE - Method for preparing methanol diesel oil microemulsion (claimed).    ADVANTAGE - The microemulsion has clear appearance and similar physical properties with pure diesel oil. Its shelf life is more than 6 months. It meets the national automotive diesel oil standard GB/T19147-2003. The additive has low toxicity and small pollution. The simple method has mild condition and low cost.
NOVELTY - Carbon dioxide gas is carbonized using oxidizing agent comprising mixture of enriched oxygen and carbon dioxide gas. The coal gas is decarbonized and the resulting mixture is subjected to carbon dioxide shift reaction to generate hydrogen and liquefied natural gas. The resulting mixture is subjected to transformation process and decarbonization process, hydrogen sulfide gas is removed, and resulting gas is subjected to methanation process to obtain refined gas. Refined gas is mixed with hydrogen, resulting gas is dehydrated and cooled to obtain liquefied methane gas and hydrogen.    USE - Processing of outward-exhausting coal gas by internal heating-type coal carbonization process used for hydrogenating coal tar and co-generating hydrogen and liquefied natural gas.    ADVANTAGE - The method economically enables processing of outward-exhausting coal gas with high efficiency and high purity.    DETAILED DESCRIPTION - Carbon dioxide gas as temperature-controlled component is subjected to coal carbonization process using oxidizing agent comprising a mixture of enriched oxygen and carbon dioxide gas. The outward-exhausting coal gas comprises hydrogen, carbon monoxide, methane, carbon dioxide and water. The coal gas is subjected to decarbonization process and the resulting mixture is subjected to carbon dioxide shift reaction to generate hydrogen and liquefied natural gas. The resulting mixture is subjected to transformation process and decarbonization process, hydrogen sulfide gas is removed, and the resulting gas is subjected to methanation process to obtain refined gas comprising carbon monoxide and carbon dioxide. Carbon monoxide and carbon dioxide gas mixed with hydrogen to obtain methane. The resulting gas is dehydrated and cooled to obtain liquefied methane gas and hydrogen.
NOVELTY - A biodiesel is prepared by heating vegetable oil and ethanol in the presence of graphite oxide catalyst, refluxing under atmospheric pressure, cooling to room temperature, filtering to separate catalyst, washing filtrate comprising mixture of product, excessive ethanol, and glycerol with saturated brine to remove ethanol and glycerol, and drying to obtain pure product; atmospheric distilling washed out ethanol and glycerol, and vacuum distilling to separate ethanol and glycerol; and washing catalyst with petroleum ether, and vacuum drying to recycle.    USE - Method for preparation of biodiesel (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has wide source of raw materials, convenient preparation and separation recovery, high activity, less dosage and heat stability of catalyst, moderate reaction condition, and reduced equipment investment.    DETAILED DESCRIPTION - A biodiesel of formula 3R-C(O)-O-CH3 and OH-CH2-C(OH)-CH2-OH is prepared by heating vegetable oil of formula R-(C)(O)-O-CH2-C-O-(C)(O)-R-(H)-CH2-O-(C)(O)-R and ethanol of formula 3CH3OH with molar ratio of 1:5-15 in the presence of 1-10 wt.% graphite oxide catalyst at 90-100 degrees C for 6-9 hours, and refluxing under atmospheric pressure, cooling to room temperature, filtering to separate catalyst, washing filtrate comprising mixture of product, excessive ethanol, and glycerol with saturated brine to remove ethanol and glycerol, and drying to obtain pure product; atmospheric distilling washed out ethanol and glycerol, and vacuum distilling to separate ethanol and glycerol; and washing catalyst with petroleum ether, and vacuum drying to recycle.    R=carbon chain fatty acid oil.
NOVELTY - Improving fuel ethanol yield involves weighing 1-3 ml fermentation substrate, adding 2 g/l ferrous sulfate (FeSO4) solution into fermentation tank, then adding 1.5-4.5 ml yeast and 10-30% Saccharomyces cerevisiae into culture medium, inoculating yeast and Saccharomyces cerevisiae at a ratio of 1:1 g to 1:3 g using 10-30 U/g cellulase, adding proper sterile water to adjust the solid-liquid mass ratio of 1:15 g in the fermenting tank, sealing the tank opening and setting the temperature at 32-40 degrees C for 60-84 hours to obtain fermentation liquid containing ethanol.    USE - For improving fuel ethanol yield (claimed).    ADVANTAGE - The present method utilizes raw material of wide source; has convenient operation; reduces the dosage of cellulase so as to reduce the process cost; and is simple.    DETAILED DESCRIPTION - Improving fuel ethanol yield by adding Fe2+ salt for simultaneous saccharification and fermentation: involves weighing 1-3 ml fermentation substrate, adding 2 g/l ferrous sulfate (FeSO4) solution into fermentation tank, then adding 1.5-4.5 ml yeast and 10-30% Saccharomyces cerevisiae into culture medium, inoculating yeast and Saccharomyces cerevisiae at a ratio of 1:1 g to 1:3 g using 10-30 U/g cellulase, adding proper sterile water to adjust the solid-liquid mass ratio of 1:15 g in the fermenting tank, sealing the tank opening and setting the temperature at 32-40 degrees C for 60-84 hours to obtain fermentation liquid containing ethanol.
NOVELTY - The apparatus (10) has a waste material feeder (30) which conveys organic waste injected to front side portion of tank form casing (20) to rear side portion of tank form casing by circulation movement of conveyance element (33). The protruding elements for diffusion are protrudingly provided to rotating shaft, and operated by rotational drive of rotary case (50). A diffusion release apparatus is set to release organic waste from discharge opening (26a) in rear side portion of tank form casing. Self-propelled apparatus (60) is connected to tank form casing down side.    USE - Organic waste diffusing treatment apparatus used in organic waste treatment facility used for carrying out fermentation decomposition treatment of organic waste such as sludge of organic refuse and sewage discharged from livestock dung and home, for manufacturing organic waste fermentation process product (claimed) such as manure. Can also be used in raw material for liquid fertilizer manufacture.    ADVANTAGE - Since the diffusion release apparatus is set to release organic waste from discharge opening in rear side portion of tank form casing, the stockyard for the temporary storage of organic waste can be reduced in size and small-scale-izing of the whole organic waste treatment facility and reduction of installed cost can be achieved easily. The cost reduction of the fermentation decomposition treatment of organic waste is attained easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of organic waste fermentation process product.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the organic waste diffusing treatment apparatus. (Drawing includes non-English language text)    Organic waste diffusing treatment apparatus (10)    Tank form casing (20)    Discharge opening (26a)    Waste material feeder (30)    Conveyance element (33)    Rotary case (50)    Self-propelled apparatus (60)
NOVELTY - Preparing carbon nanotube graphene composite material includes directly mixing uniformly dispersed carbon nanotubes and a catalyst for graphene, causing the graphene to grow in situ in a carbon nanotube network by chemical vapor deposition, and removing the catalyst after purification treatment to obtain the carbon nanotube graphene composite material.    USE - Method for preparing carbon nanotube graphene composite material used as electrochemical energy-storing material, catalyst carrier material, transparent conductive thin film material, reinforcing material, conductive material and adsorption and desorption material (claimed).    ADVANTAGE - The method has simple operation, low cost and easy industrial production.    DETAILED DESCRIPTION - Preparing carbon nanotube graphene composite material comprises:    (A) preparing uniformly dispersed carbon nanotube suspension in deionized water or organic solvent, where the content of the carbon nanotube is 0.01-2 mass%;    (B) adding the carbon nanotube to the carbon nanotube suspension which is 1-10 times of the magnesium oxide catalyst, and uniformly mixing the mixture to form uniform and stable suspension;    (C) adding the mixture suspension by filtering method for separating, drying, and uniformly mixing to obtain the carbon nanotube and mixed powder of magnesium oxide catalyst to obtain the carbon nanotube or magnesium oxide catalyst supporting a thin film;    (D) mixing the carbon nanotube and mixture powder of magnesium oxide catalyst by supporting the film in an inert gas at 500-600 degrees C;    (E) continuously raising the calcined sample to 800-1000 degrees C, introducing carbon source, and after high temperature chemical vapor deposition for 5 minutes-2 hours, obtaining the formed product; and    (F) dissolving the formed product in an acid to remove magnesium oxide catalyst to obtain the carbon nanotube after drying-graphene composite material.
NOVELTY - Naproxcinod intermediate S-2-(6-methoxy-2-naphthyl)-4-chlorobutyl propanoate is prepared by heating naproxen in cyclohexane to dissolve, adding 4-chloro-1-butanol, cooling to low temperature, and dropping concentrated sulfuric acid under reflux condition; after reaction, cooling to low temperature, and dropping concentrated sulfuric acid under reflux condition; and cooling to room temperature, washing reaction product with 2% sodium hydroxide solution and water, drying over anhydrous magnesium sulfate, filtering, concentrating filtrate, decompressing and drying to obtain white crystal.    USE - Method of preparing naproxcinod intermediate S-2-(6-methoxy-2-naphthyl)-4-chlorobutyl propanoate (claimed).    ADVANTAGE - The method is suitable for mass production, and utilizes cyclohexane which is environmentally friendly and safe to health of workers.    DETAILED DESCRIPTION - Preparation of naproxcinod intermediate S-2-(6-methoxy-2-naphthyl)-4-chlorobutyl propanoate comprises heating naproxen in cyclohexane to dissolve, adding 4-chloro-1-butanol, cooling to low temperature, and dropping concentrated sulfuric acid under reflux condition; after reaction, cooling reaction system to low temperature, and dropping concentrated sulfuric acid under reflux condition; and after finishing reaction, cooling reaction system to room temperature, washing reaction product with 2% sodium hydroxide solution for 3 times, then washing with water for 3 times, drying over anhydrous magnesium sulfate, filtering, concentrating the filtrate, decompressing and drying to obtain white crystal.
NOVELTY - Synthesis of 3-(N,N-diallyl)amino-4-methoxy acetanilide comprises mixing 3-amino-4-methoxyacetaniline and water, adding dispersant, and stirring for pulping; and adding hydrocarbon reagent and acid binder to carry out alkylation. The acid binder is sodium hydroxide aqueous solution or sodium hydroxide. The reagent is allyl chloride.    USE - Method for synthesizing 3-(N,N-diallyl)amino-4-methoxy acetanilide (claimed) used as dye coupling component.    ADVANTAGE - The method is simple and environment-friendly, saves energy, and has low cost.
NOVELTY - Enteromorpha hydrothermal liquefaction comprises crushing dried strip enteromorpha in plant crusher to crushing, packing into bottle seal, storing in refrigerator, adding 2-5 g enteromorpha powder and deionized water in reaction kettle, sealing tightly, sealing reaction kettle into molten salt at 370 degrees C, adding 20wt.% potassium carbonate catalyst, and reacting for 40 minutes.    USE - Method of enteromorpha hydrothermal liquefaction used for preparation of bio-oil (claimed).    ADVANTAGE - The method has mild reaction condition.
NOVELTY - Biomass comprehensive conversion device comprises biomass multifunctional integrated conversion device (1), gas purifying and separating device (2), liquid standing separation device (3), gas purifying device (4), gas storage device (5), hot water collecting tank (6), and water storage tank (7). The biomass carbonizing, gasifying, pyrolysis and other processes are integrated to realize waste resource comprehensive utilization and conversion.    USE - Biomass comprehensive conversion device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass comprehensive conversion method comprising placing raw materials in biomass pyrolysis device, where thickness of biomass is 3/4 of device height, carrying out ignition combustion, adding straw 20-30 cm, carrying out combustion of straw layer, opening pneumatic device, continuously feeding 20-30 cm biomass, producing bio-char, and mixed gas; mixed gas entering into biological filter, obtaining pure mixed gas, entering gas separator and gas condensing liquid standing separation device; non-condensable gas flowing to gas purifying device, condensing liquid standing in liquid standing separation equipment, wood vinegar entering into acid tank through acid outlet, biological tar entering into tar pool by tar outlet, and non-condensable gas entering gas purifying device, washing, rinsing, bubbling washing, gas-liquid separating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass comprehensive conversion device (Drawing includes non-English language text).    Biomass multifunctional integrated conversion device (1)    Gas purifying and separating device (2)    Liquid standing separation device (3)    Gas purifying device (4)    Gas storage device (5)    Hot water collecting tank (6)    Water storage tank (7)
NOVELTY - Biomass comprehensive transformation device comprises pyrolysis tank (1), tri-state purifying and separating device (2), standing separating device (3), gas purifying device (4), and gas storage tank (5). The gas purifying device further comprises pneumatic device (6), cyclone separator (21) and dust remover (22), where pneumatic device is connected with tri-state purification and separation device, cyclone separator is connected with pyrolysis tank, and dust remover is connected with purifying and separating device.    USE - Biomass comprehensive transformation device.    ADVANTAGE - The biomass conversion rate is 0.5-1.5 t/hour.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass comprehensive transformation device.    Pyrolysis tank (1)    Tri-state purifying and separating device (2)    Standing separating device (3)    Gas purifying device (4)    Gas storage tank (5)    Pneumatic device (6)    Cyclone separator (21)    Dust remover (22)
NOVELTY - Methanol gasoline comprises 70-80% methanol, 10-15% ethanol, 2-5% n-propanol, 5 to 10% n-butanol, 2-5% isopropanol, 0.05-0.1 g/L t-butyl acetate, and 0.016-0.032 g/L nanoscale ferrocene mixture.    USE - Methanol gasoline composition.    ADVANTAGE - The methanol gasoline is low cost and environment friendly, can reach 93 performance standards and indicators of gasoline, and has good market prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of methanol gasoline comprising adding the proportioned raw materials to a reaction cylinder, stirring with anti-explosion rod at room temperature for 0.5-1 hour, and standing for 1 hour.
NOVELTY - A biological acidification oil-modified fuel comprises 90-96 pts. wt. biological acid oil, 6-10 pts. wt. alcohol, 1-3 pts. wt. dispersant and 0.4-1 pts. wt. synthetic agent.    USE - Biological acidification oil-modified fuel.    ADVANTAGE - The fuel is pollution-free, low in cost and environment-friendly has high combustion heat value, good fluidity, almost zero discharge and combustion, and can make full use of palm oil refinery emissions of waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological acidification oil-modified fuel by mixing raw materials, high speed shearing, subjecting to step-by-step ultrasonic treatment at frequency of 2x 104 Hz, 2x 105 Hz and 2x 106 Hz, and filtering, storing filtrate in a tank, and storing residues in the residue tank.
NOVELTY - Methanol gasoline comprises 85-90% methanol, gasoline, methyl tert-butyl ether, 1-octanol, pentaerythritol, tetrahydrofuran, 1,4-butanediol, isoamyl alcohol, n-butanol, isopropanol, benzene, dimethyl carbonate, Tween-20 (RTM: polyoxyethylene (20) sorbitan monolaurate), Span-60 (RTM: sorbitan monostearate), lead acetate, acetyl benzylamine and silicon aluminum phosphate.    USE - Methanol gasoline used as gasoline alternative.    ADVANTAGE - The methanol gasoline has good stability, high combustion, high heating value, no smell, low smoke emission, simple preparation and low operation cost. It reduces carbon monoxide emissions and sulfur content.    DETAILED DESCRIPTION - Methanol gasoline comprises 650-700 pts. wt. 85-90% methanol, 260-300 pts. wt. 93# gasoline, 1-5 pts. wt. methyl tert-butyl ether, 1-4 pts. wt. 1-octanol, 1-4 pts. wt. pentaerythritol, 1-2 pts. wt. tetrahydrofuran, 1-3 pts. wt. 1,4-butanediol, 1-6 pts. wt. isoamyl alcohol, 1-5 pts. wt. n-butanol, 1-4 pts. wt. isopropanol, 1-5 pts. wt. benzene, 1-3 pts. wt. dimethyl carbonate, 1-3 pts. wt. Tween-20 (RTM: polyoxyethylene (20) sorbitan monolaurate), 1-3 pts. wt. Span-60 (RTM: sorbitan monostearate), 0.5-1.5 pts. wt. lead acetate, 0.5-3 pts. wt. acetyl benzylamine and 0.5-1.2 pts. wt. silicon aluminum phosphate. An INDEPENDENT CLAIM is included for the preparation of methanol gasoline comprising mixing methanol solution, methyl tert-butyl ether and 1-octanol under room temperature and 60-70% air humidity, uniformly stirring to obtain mixed solution; adding pentaerythritol, tetrahydrofuran, 1,4-butanediol, isoamyl alcohol, n-butanol, isopropanol, benzene, calcium carbonate, Tween-20 (RTM: polyoxyethylene (20) sorbitan monolaurate), Span-60 (RTM: sorbitan monostearate), acetyl benzylamine, silicon aluminum phosphate and 93# gasoline, uniformly stirring to obtain mixed solution (ii); and stirring mixed solution (ii) for 30-50 minutes, and standing for 10 hours.
NOVELTY - Environment-friendly and energy-saving micro-carbon alcohol oil comprises water, mixed alcohol, 0.1-0.3 wt.% catalyst, 0.05-0.1 wt.% sugar, 0.05-0.1 wt.% salt, 0.2-0.4 wt.% petroleum ether, 0.2-0.4 wt.% ethylene glycol monobutyl ether, 0.4-0.5 wt.% acetone, 0.8-1 wt.% cotton seed oil and 0.02-0.05 wt.% triethylamine. The water and mixed alcohol are mixed at 50:50 mass ratio. The weight percentages of catalyst, sugar, salt, petroleum ether, ethylene glycol monobutyl ether, acetone, cotton seed oil and triethylamine are based on total weight of water and mixed alcohol mixture.    USE - Environment-friendly and energy-saving micro-carbon alcohol oil.    ADVANTAGE - The micro-carbon alcohol oil has 550-7000/ton heating value. It saves carbon oil consumption.
NOVELTY - Regeneration of hydrogen-carbon (H-C) single oxygen (O) power fuel comprises using biomass C electrode in vacuum underwater arc, splitting water molecules to obtain H and O ions, reorganizing H,C and O within the plasma region to form bubbles and floating water surface, and compressing.    USE - Regeneration method of hydrogen-carbon (H-C) single oxygen (O) power fuel (claimed).    ADVANTAGE - The use of vacuum zero-point energy generate isotope of hydrogen instead of acetylene cutting completely the different effect on the nature of the metal, pure hydrogen and oxygen explosion and combustion and has stable performance. The fuel has purity of 99.99%, has carbon monoxide content which is harmless, can be stored for a long period of time and can still maintain the original fuel efficacy. The method solves the problems of normal nonrenewable energy resource such as environment pollution, high cost of new energy and not using renewable biomass carbon dioxide and water. The biomass carbon source and water is clean, has low production cost, strong practicability, and can replace conventional energy of new fuel.
NOVELTY - A liquefied natural gas (LNG) is prepared by introducing coal-based synthesis gas comprising hydrogen and carbon monoxide in methanation reactor, dividing gas into two streams, and mixing first stream comprising coal-based synthesis gas, recycled gas and/or circulating liquid in methanation reactor; mixing second stream of coal-based synthesis gas and methanation reactor outlet gas, introducing into second stage methanation reactor, passing through third and fourth stage methanation reactors to obtain rich methane gas; and decarburizing, preferably wet or dry decarburizing, and liquefying.    USE - Method for preparation of liquefied natural gas (claimed).    ADVANTAGE - The method has low ratio of hydrogen and carbon monoxide and production cost, improves utilization rate of effective gas and reduces carbon monoxide content in the product gas.    DETAILED DESCRIPTION - A liquefied natural gas (LNG) is prepared by introducing coal-based synthesis gas comprising hydrogen and carbon monoxide with molar ratio of 1.6-2.3 in methanation reactor, dividing gas into two streams, and mixing first stream comprising coal-based synthesis gas, recycled gas and/or circulating liquid with temperature of 200-300 degrees c in methanation reactor; mixing second stream of coal-based synthesis gas and methanation reactor outlet gas, introducing into second stage methanation reactor, passing through third and fourth stage methanation reactors to obtain rich methane gas; and decarburizing, preferably wet or dry decarburizing, and liquefying. The methanation reactor and second stage methanation reactor is equipped with dual function catalyst comprising 10-60 wt.% carrier, 1-15 wt.% nickel, 1-15 wt.% cobalt, 1-15 wt.% molybdenum and 1-5 wt.% additive for methane synthesis and water gas shift.
NOVELTY - Isomerization reaction of straight-chain paraffin comprises placing straight-chain paraffin raw material into reactor, in the presence of hydrogen with isomerization catalyst contact and reacting to generate branched alkane. The isomerization catalyst is loaded with hydrogenation/dehydrogenation metal component and solid super-acid. The solid super acid is metal oxide loaded with perchlorate (ClO4-) radical. The hydrogenation/dehydrogenation metal component is platinum (Pt), palladium (Pd) and/or nickel (Ni).    USE - Method for isomerization reacting straight-chain paraffin (claimed).    ADVANTAGE - The method has low reaction temperature, high conversion rate, and good selectivity.
NOVELTY - Preparation of amlodipine maleate comprises adding maleic acid amlodipine free base in water to obtain amlodipine maleate crude product, and refining crude amlodipine maleate to obtain maleic acid amlodipine besylate.    USE - Method of preparation of amlodipine maleate (claimed).    ADVANTAGE - The method takes water as reaction medium, has low cost, is environment-friendly, and reduces generation of impurity in synthesis process.
NOVELTY - Low-temperature oil and gas condensate absorption and production of ethanol gasoline comprises taking absolute ethyl alcohol absorbing agent after cooling, pumping powered by gas-liquid two-phase flow pump, pumping cooling oil and water, dispersing oil in low temperature ethanol in micro-bubble form, cooling, dissolving oil in ethanol under pressure, processing oil gas condensation-absorption recycling, and gas mixture of ethanol and gasoline to obtain ethanol gasoline.    USE - Method of low-temperature oil and gas condensate absorption and production of ethanol gasoline (claimed) used for gas station.    ADVANTAGE - The method has simple process, utilizes few devices, and has high oil gas recovery rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of low-temperature oil and gas condensate absorption and production of ethanol gasoline.
NOVELTY - Methane and carbon dioxide are extracted and purified from marsh gas by purifying marsh gas; preparing methane gas and carbon dioxide gas bottle with suction device to separate both gases, with pressure of less than 10 Pa; cooling the separated chamber; inputting purified marsh gas in the chamber; heating to room temperature to separate pure methane and pure carbon dioxide; taking pure methane in methane gas bottle and pure carbon dioxide into carbon dioxide gas bottle; and extracting methane and carbon dioxide.    USE - Method for extracting pure methane and carbon dioxide from marsh gas (claimed).    ADVANTAGE - The method improves marsh gas composition accumulation rate that can be extracted with high purity.    DETAILED DESCRIPTION - Extracting and purifying methane and carbon dioxide from marsh gas comprises:    (A) purifying marsh gas before extracting methane and carbon dioxide, and removing impurity and water vapor;    (B) preparing methane gas and carbon dioxide gas bottle with suction device to separate both gases, with pressure of less than 10 Pa;    (C) cooling the separated chamber;    (D) inputting purified marsh gas in the chamber;    (E) heating to room temperature to separate pure methane and pure carbon dioxide;    (F) taking pure methane in methane gas bottle and pure carbon dioxide into carbon dioxide gas bottle; and    (G) extracting methane and carbon dioxide.    An INDEPENDENT CLAIM is included for a device for extracting and purifying methane and carbon dioxide from marsh gas.
NOVELTY - The invention provides a serial-type heating transport reaction device applied for an organic fertilizer production, including two tank chambers, mixing shafts respectively installed in the tank chambers and provided with a helical blade thereon, and a driving motor. Each of the tank chambers is provided with a containing space and an opening, in which the containing spaces of the tank chambers are mutually connected to form a communicated mixing containing chamber, and the openings of the tank chambers are capable of being correspondingly joined. The mixing shafts installed in the containing spaces of the tank chambers are connected to each other and linked to the driving motor, and each of the tank chambers is configured with a heater and a reagent supply device. Accordingly, the purpose of transporting a material located in the mixing containing chamber from one tank chamber toward the other tank chamber can be achieved.
NOVELTY - Device for firing up of longitudinal shape from wood of coniferous or deciduous rock, comprises section in the form of polygon or circle and has lateral surface containing incipient from n number of radial cannelures, where each section has length l2, and n is 4, 6 or 8.    USE - For firing up of longitudinal shape from wood of coniferous or deciduous rock or deciduous species (claimed).
NOVELTY - The apparatus has a generator (1) and a pulse nonlinear amplifier (2) that are controlled by an output filter (3). A hydrogen resonant generator (4) is connected to a processor (5) to run a facility.    USE - Apparatus for generating hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for generating hydrogen.    Generator (1)    Pulse nonlinear amplifier (2)    Output filter (3)    Hydrogen resonant generator (4)    Processor (5)
NOVELTY - Method for composting involves mixing linear horizontal displacement, where organic material is piled up to form linear carries that are mechanically mixed by tumbling with stems.    USE - Method for composting (claimed).    ADVANTAGE - The composting method takes less time to produce compost.
NOVELTY - The metal supported solid oxide fuel cell comprises an electrode layer, in which an electrolyte layer is formed on one side of a cell. A porosity metal supporter is plated and united with the electrolyte layer. An electroplating process is possible with plating adhesion, which is made of nickel plating liquid. The electrode layer is made of yttria-stabilized zirconia nickel where the composition of nickel oxide and yttria-stabilized zirconia is reduced.    USE - Metal supported solid oxide fuel cell for generating power.    ADVANTAGE - The metal supported solid oxide fuel cell comprises an electrode layer, in which an electrolyte layer is formed on one side of a cell and porosity metal supporter is plated and united with the electrolyte layer, thus easily welds the metal supporter and electrode without the need for separate thermal process, improves the cohesive power and the shrinkage ratio, and also removes the diffusion problem and heat treatment atmosphere problem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a metal-supported solid oxide fuel cell fabricating method involves forming porosity metal supporter that is made of stainless mesh.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a metal supported solid oxide fuel cell fabricating method. (Drawing includes non-English language text).
NOVELTY - The device has a magnetic separator (40) to embellish ferrous metal material foreign substance from the waste. A non-ferric selector (50) selects the nonferrous metal foreign substance among the waste. A grain size screen (60) is provided with specific particle size to select the small soil and moisture among the waste filtered with nonferrous metal foreign substance.    USE - Waste separating device for solid material bio-fuel production equipment (claimed).    ADVANTAGE - The high-quality refuse derived fuel production can be ensured. The production of solid material bio-fuel with excellent calorific value can be achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a solid material bio-fuel production equipment; and    (2) a solid material bio-fuel production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid material bio-fuel production equipment.    Magnetic separator (40)    Non-ferric selector (50)    Magnet (56)    Grain size screen (60)    Collecting container (70)
NOVELTY - Compost comprises bamboo sawdust, freshwater shellfish powder and bone meal.    USE - The compost is useful as fertilizer for plants, forest products (including herbs e.g. wood-cultivated ginseng, Codonopsis lanceolata Traut, Platycodon grandiflorum or polygoni multiflori radix, wild plants e.g. wild garlic, Aralia elata Seemann, chwinamul, Pimpinella brachycarpa, Ligularia fischeri, Youngia sonchifolia Maxim., bog rhubarb, fernbrake, Cirsium setidens or Allium victorialis, and coniferous or broad-leaved trees), and agricultural plants (strawberry, tomato or red pepper) (all claimed).    ADVANTAGE - The compost provides high survival rate and growth of forest and agriculture plants as it is supplemented with inorganic components; and is comfortable to transport and scatter in the forest lands without washing away as it is in the form of pellet or polyhedron shape, and suitable for acidic forest soils.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing the compost, comprising mixing bamboo sawdust, freshwater shellfish powder and bone meal to obtain a mixture, and molding the obtained mixture.
NOVELTY - A sulfur-free rhizoma gastrodiae extract is produced by washing fresh rhizoma gastrodiae; extracting large size fresh rhizoma gastrodiae for 24-26 minutes, extracting medium size for 18-22 minutes, or extracting small size for 14-16 minutes; and drying large at 50-60 degrees C for 24 hours for 6-7 times, medium size for 5-6 times, or small size for 4-5 times.    USE - Method of producing a sulfur-free rhizoma gastrodiae extract (claimed).    ADVANTAGE - The production method has high production efficiency and high yield, produces product having high nutrient content can be applied to industrial production, and is simple, low cost, energy-saving and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of planting rhizoma gastrodiae comprising selecting land; selecting semi-female half grown rhizoma gastrodiae plant; adding activated carbon, straw ash, potash fertilizer, and phosphogypsum having a ratio of 4:5:2:8-10; cultivating for 2-3 months in a pit; paving a layer comprising 12-16 mass% grass carbon, 20-30 mass% tobacco leaf foam, 0.4-0.6 mass% microelement, 13-18 mass% biogas residue, 0.4-0.6 mass% chitin, 3-5 mass% pyroligneous, and 0.8-1.5 mass% mixture of river sand and bacteria; covering; weeding; adding 5-10 pts. wt. slow release urea, 3-5 pts. wt. potassium chloride, 10-15 pts. wt. monocalcium phosphate, 2-3 pts. wt. ferrous sulfate, 0.5-1 pts. wt. borax and 0.2-0.3 pts. wt. ammonium dihydrogen phosphate; cultivating; spraying an insect-preventing agent; and drying.
NOVELTY - Manufacturing porous organic-metallic frame body, comprises dissolving organic ligand precursor and metal salt including 1-16 group metal ion and 14-17 group anion in a first solvent to form porous metal-organic backbone, dipping the backbone in a second solvent, and immersing porous metal-organic backbone in a third solvent using supercritical carbon dioxide and then drying.    USE - The method is useful for manufacturing porous organic-metallic frame body, which is useful in a micromolecule absorber such as carbon dioxide absorber, methane absorber and hydrogen absorber (all claimed), gas preservation, catalyst, sensor and ion exchange process field.    ADVANTAGE - The method is capable of efficiently and rapidly manufacturing the porous organic-metallic frame body with good hydrophobicity or hydrophilicity and mass production.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a method for manufacturing a porous organic-metallic frame body (Drawing includes non-English language text).
NOVELTY - Glycerol based heterogeneous solid base catalyst (I) comprising a 6-7.25% of sodium is new, where (I) is insoluble in water and organic solvent like chloroform, hexane, acetone, methanol, ethanol, isopropanol, toluene, benzene, pyridine and N,N-dimethylformamide and reusable.    USE - (I) is useful for the transesterification of vegetable oils (including sunflower oil, high oleic sunflower oil, soybean oil, palm oil, castor oil or rice bran oil), and preparing the biodiesel (all claimed), which is useful as a substitute for petroleum diesel fuel.    ADVANTAGE - (I) has high moisture tolerance capacity and transesterification activity; and can be easily prepared under mild reactive conditions in an economical manner. The two step process provides biodiesel without using sulfuric acid and alkali solution, hence it is environmental friendly.    DETAILED DESCRIPTION - Glycerol based heterogeneous solid base catalyst (I) compound of formula (CH(0.70-0.82)S(0.015-0.02)O(0.79-0.84)) (Ia) with 6-7.25% of sodium is new, where (I) is insoluble in water and organic solvent like chloroform, hexane, acetone, methanol, ethanol, isopropanol, toluene, benzene, pyridine and N,N-dimethylformamide and reusable. INDEPENDENT CLAIMS are included for:    (1) preparing (I);    (2) a process-II for preparing a biodiesel by transesterification of vegetable oils using (I), comprising reacting vegetable oil with alcohol, preferably methanol in a mole ratio of 1:6-1:40 in the presence of solid base catalyst at a temperature of 30-65 degrees C for 1-16 hours, preferably 2-5 hours; and    (3) a two step process for biodiesel production from high free fatty acid containing non-edible oils and animal fat comprising Jatropha oil, karanja oil, deodorizer distillate or used oils, by esterification of free fatty acid using glycerol based carbon acid catalyst followed by transesterification of biodiesel using carbon based base catalyst.
NOVELTY - A soil modifying agent comprises soil modifying agent comprises total nutrient including nitrogen, phosphorus pentoxide and potassium oxide, organic matter and water, where the total nutrient weight ratio is 1.8-2.5%, where the organic matter weight ratio is 70-73%, and the water content weight ratio of 25-35%.    USE - As soil modifying agent (claimed).    ADVANTAGE - The soil modifying agent uses bark, farmyard manure, photosynthetic bacteria liquid and water, and obtains the produced organic medium by a simple process comprising high molecular weight, in water preserving property, good air permeability of soil modifying agent, which can be applied to planting greenhouse vegetables, fruit tree tobacco planting, gardening lawn and garden greening. The soil modifying agent, improved capacity as the existing soil modifying agent for more than three times, then using the soil, soil structure, physical and chemical performance, high rate of emergence, growth, high yield production oil improvement agent. The method is simple and easy to operate, the raw material is cheap and easy to obtain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing soil modifying agent involving crushing and sieving the bark crushing part diameter is 4 to sift out into bark block; preparing fertilizer raw material stack fertilizer stack raw material comprises bark of 60-80 pts. wt.% of farmyard manure, 10-20 pts. wt.% of photosynthetic bacteria liquid is 2-5%, water 8-15%; bulk fertilizer pile the fertilizer stack is piled raw material 200% of the total weight to 500 of stack; turning the fertilizer pile to ferment, testing fertilizer stack internal temperature, when the temperature is 60-70 degrees C, overturning for one time, repeating for 8 to 12 times until the temperature is not raised; sieving and packaging.
NOVELTY - Synthesis of 17 steroidal carboxylic acid ester (II) as key intermediate for 17 corticosteroid acylated hydroxy steroid drug, involves: dissolving corticosteroid based cyclic ortho ester (I) in solvent A containing 50 wt.% aqueous solution of gluconic acid as catalyst, and then adding solvent B, at -20 to 50 degrees C, reacting for 0.5-48 hours to obtain the compound (II), where the solvent A containing 50 wt.% aqueous solution of gluconic acid, and the solvent B has volume ratio of 1:0.1-5.    USE - For synthesis of steroidal carboxylic acid ester as key intermediate for 17 corticosteroid acylated hydroxy steroid drug (claimed).    ADVANTAGE - The aqueous solution of gluconic acid with recyclable catalyzed hydrolysis, effectively reduces the use of organic solvents and reagents. The method reduces costs; reduces pollution; and is a simple synthesis method.    DETAILED DESCRIPTION - Synthesis of 17 steroidal carboxylic acid ester of formula (II) as key intermediate for 17 corticosteroid acylated hydroxy steroid drug, involves: dissolving corticosteroid based cyclic ortho ester of formula (I) in solvent A containing 50 wt.% aqueous solution of gluconic acid as catalyst, and then adding solvent B, at -20 to 50 degrees C, reacting for 0.5-48 hours to obtain the compound (II), where the solvent A containing 50 wt.% aqueous solution of gluconic acid and the solvent B has volume ratio of 1:0.1-5.    a=single bond or a double bond;    R1=H, CH3, C2H5, C3H7 or C4H9;    R2=CH3, C2H5, C3H7 or C4H9;    X1=H or F;    X2=H, F or CH3;    X3=H or CH3.
NOVELTY - The furnace has a drying chamber (31) whose furnace wall is provided with a fireproof layer (36), a heat insulating layer (35) and a shell (34). The fireproof layer is provided with an annular gas-distributing chamber (32), a cavity (33) and an annular gas collecting chamber (38). The annular gas collecting chamber is arranged on an upper part of the cavity. The drying chamber is connected with a gasification furnace body (18). The gasification furnace body is provided with a plasma spray gun (11) that is provided with an opening. A spiral pusher is extended in the gasification furnace body.    USE - Gasification furnace for performing biomass rubbish treatment.    ADVANTAGE - The furnace avoids dioxin pollution problem, improves gasification-liquefying production line, converts household rubbish into methanol product, achieves zero discharge property and treats domestic rubbish without pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a gasification furnace for performing biomass rubbish treatment in partial section.    Plasma spray gun (11)    Gasification furnace body (18)    Drying chamber (31)    Annular gas-distributing chamber (32)    Cavity (33)    Shell (34)    Heat insulating layer (35)    Fireproof layer (36)    Annular gas collecting chamber (38)
NOVELTY - Treating pig manure, comprises separation of pig excrement into dry dung and manure, dry fermentation of manure, where the first part of manure is discharged into marsh gas tank, and the second part of manure is discharged into the sedimentation tank for sedimentation, sterilizing, disinfecting and washing precipitated piggery manure.    USE - The fermented pig manure is useful for the production of organic fertilizer and fish feed (claimed).    ADVANTAGE - The method treats pig manure in a cost-effective and eco-friendly manner.
NOVELTY - Hydrolyzing saponin from yellow ginger involves taking yellow ginger, crushing, grinding, and adding water into it to obtain yellow ginger slurry, adding organic acid or inorganic acid to regulate slurry pH of 1-6, adding organic matter hydrolyzing auxiliary agent to subcritical hydrolysis, where the temperature of subcritical hydrolysis is 60-270 degrees C, pressure is 30 Mpa, and hydrolysis time is 1 hour, after finishing the subcritical hydrolysis, taking out slurry, filtering, washing, drying, gasoline reflux extracting for 4 hours, and then cooling and crystallizing to obtain the saponin.    USE - For hydrolyzing saponin from yellow ginger (claimed).    ADVANTAGE - The present method does not produce high concentration acid waste water; provides saponin having high yield and good quality; is stable; can be repeatedly use; has low production cost; has low industrial production device investment; can greatly reduce the energy consumption and water consumption; and is good for popularization and application.
NOVELTY - A kind of new-type biomass ball stove, comprising a steam pipe, a fan, a water tank and an annular air duct, the fan is connected with the upper part on the outer wall of the furnace body on the lower part of the furnace body, the water tank through air inlet pipe, the upper part of the water tank is provided with a water inlet, the lower part with an outlet valve, the steam pipe is installed on the bottom of the furnace body on the upper part of the furnace body, the annular air guide pipe. This utility model has simple structure, low cost, convenient use, small consumption, obvious energy saving effect, clean and sanitary, high heat value, the operation is safe, the service life of the device is long, and without smoke and dust pollution.
NOVELTY - This utility model claims a straw gasification furnace, comprising a furnace body, a stirring rod, a stirring head, a rod, a supporting column, a rotary motor, a baffle block, a receiving plate and a handle, the upper part of the furnace body is provided with a stirring rod, the stirring rod is connected with the stirring head, lower part inside of the furnace body is provided with a stirring rod, the stirring rod is connected with the rotating motor, the bottom of the furnace body is provided with a supporting column. This utility model has simple structure, smart design, is provided with a stirring device to make the fuel burn completely, it will not appear the phenomenon of flameout in burning process of waste residue can pass through device for automatic cleaning, it saves time, and is provided with a special receiving device of cleaning ash is simple and convenient.
NOVELTY - Fluidized bed biomass gasification furnace dust collecting heat pre-heating fuel device relates to biomass gasification furnace. A secondary cyclone dust collector (5), the first level cyclone dust collector (6), a spiral feeding machine (14), a secondary cyclone dust collector (5) and the inner wall of the sleeve A (2), the inner wall is welded with a fin A (3) and the outer wall of the first level cyclone dust collector (6) is sleeve B (8), the inner wall is welded with a fin B (9), spiral feeding machine (14) and the inner wall of the jacket (13), a cold water replenishing water pipe (4) outlet B of the sleeve A (2), A (2), the upper part of the steam outlet A (1) B (8) jacket steam inlet B of the lower part (10), B (8), the upper part (7) is connected to the spiral feeder (14) of the jacket (13) upper part of the front end of the first steam inlet C (11), C (13), the other end of the lower part is provided with a water outlet (12). Is provided with simple and compact structure, convenient manufacture and assembly, which is good for heat right to be used as fuel, the waste heat recycling effect and so on.
NOVELTY - This utility model claims a kind of new biomass gasification agent controller, the controller comprises a flame arrester and a controller main body, a flame arrester is provided with a first air outlet pipe, wherein the controller main body is provided with two charging air inlet pipe of a oxidizing agent, the two air inlet pipe are connected with the air outlet pipe, the air inlet pipe and the two are provided with a control switch and a separated air inlet channel, the air outlet pipe is provided with a control switch, the controller main body is provided with an exhaust pipe and a gas outlet pipe; After adopting said technical plan, this utility model has simple and rational structure, convenient and fast use, two different gasification agent is isolated and so on.
NOVELTY - Preparing ferment biological organic fertilizer involves mixing sludge, plant waste and high temperature aerobic bacteria, where the obtained mixture for stacking fermentation until the mixture moisture content reduced to 40 wt.%, and then the stacking fermentation product after curing, where the sludge with plant waste material of which the weight ratio is 1:3-2 to each kilogram of the implant; adding amount of the high temperature resistant aerobic bacteria is 1.25-2.5 hundred million, the aerobic bacteria at least can bear the temperature is 50 degrees C.    USE - For preparing ferment biological organic fertilizer (claimed).    ADVANTAGE - The method uses sludge and plant waste yeast for preparing microbial organic fertilizer, which not only solves the problem that the sludge and plant waste resource utilization is difficult, but also solves the problem that the bio-organic fertilizer shortage problem, and it has wide application prospect, the bio-organic fertilizer has high fertilizer effect, and has great economic benefit and social benefit.    DETAILED DESCRIPTION - Preparing ferment biological organic fertilizer involves mixing sludge, plant waste and high temperature aerobic bacteria, where the obtained mixture for stacking fermentation until the mixture moisture content reduced to 40 wt.%, and then the stacking fermentation product after curing, where the sludge with plant waste material of which the weight ratio is 1:3-2 to each kilogram of the implant. The weight ratio of a reference to each kilogram of plant waste, the adding amount of the high temperature resistant aerobic bacteria is 1.25-2.5 hundred million, the aerobic bacteria at least can bear the temperature is 50 degrees C.
NOVELTY - Forming bioorganic fertilizer involves: mixing leftovers of waste fungus rod/mushroom stick and straw of edible fungi, followed by mixing with raw lime powder, covering with a degradable agricultural film at high temperature for 1-2 months to ferment; opening the stack, uniformly mixing it with ectotrophic mycorrhizal (EM) fungi, to obtain semi-spherical stacked material; and mixing soil and rice husk, adding water and stirring to obtain mud, coating the mud with semi-spherical stacked material, then drying by using air heat preservation fermenting for 3-5 months.    USE - For producing bioorganic fertilizer (claimed) which is useful for crops such as rice, wheat and corn.    ADVANTAGE - The present method is simple, low-cost, fully utilizes the waste and straw, is environment-friendly and at the same time gave farmer a biological organic fertilizer.    DETAILED DESCRIPTION - Producing bioorganic fertilizer involves: uniformly mixing leftovers of waste fungus rod or mushroom stick and straw of edible fungi according to mass ratio of 1:3-1:5, followed by mixing with raw lime powder at mass ratio of 200:1-400:1, to obtain semi-spherical stack having diameter of 2-3 m and height of 1-2 m, and fermenting stack by covering it with a degradable agricultural film at high temperature for 1-2 months; opening the stack, then uniformly mixing the stack with ectotrophic mycorrhizal (EM) fungi at a mass ratio of 200:1-300:1, to obtain semi-spherical stacked material having diameter of 2-3 m and height of 1-2 m; and uniformly mixing soil and rice husk at mass ratio of 20:1-50:1, adding water and stirring to obtain mud, coating the mud with semi-spherical stacked material, and drying the peripheral soil using air heat preservation fermenting for 3-5 months to generate biological organic fertilizer.
NOVELTY - The method involves extending residual natural combustible residence time in a furnace body. Tar cracking process is carried at high temperature to release residual heating energy of the furnace body. The furnace body is provided with a gas pipe.    USE - Method for performing high heat value low tar household biomass gasification.    ADVANTAGE - The method enables releasing remaining energy and improving a furnace heating value and lower tar emissions to meet requirement of a household-type cooker.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating operation of high heat value low tar household biomass gasification.'(Drawing includes non-English language text)'
NOVELTY - The utility model claims a new-type oil-absorbing type biomass straw gasification furnace, comprising a generating tank and the upper cover, the inner side wall of the barrel body is transversely provided with a first annular ring, the first annular retaining ring is provided with distance with the upper edge of the upper cylinder and the upper inner side edge of the first vertical annular retaining ring is provided with a second annular ring, the cylinder inner side, the first annular ring and second annular ring to form an annular groove, the upper cover and the cylinder body by an annular ring is embedded in the annular groove, the lower bottom of the annular cylinder is provided with a plurality of oxygen inlet pipe, the lower bottom of the cylinder is provided with at least one side wall of the lower end of the ash outlet, the upper and lower edge of the cylinder extends into the cylinder body and a certain distance to form an annular air channel and the lower inner wall of the cylinder body, the lower cylinder body is provided with an air outlet, the air outlet is connected with the annular air outlet channel. A kind of the new type biomass straw gasification furnace, the ignition is fast, the fire power is strong, the service life is long, a lid feeding smokeless non flameout, low cost and no pressure design is convenient and safe to operate, energy-saving and environment-friendly.
NOVELTY - A kind of biomass gasification furnace tar separator, comprising a is connected with the air inlet pipe and the air outlet pipe of the shell, there is 1-5 of dividing wall water-cooling heat exchanger in the shell, a dividing wall water-cooling heat exchanger of the cooling water pipe is bent into curved shape is fixed on the steel plate, the dividing wall water-cooling heat exchanger and the shell gas flow space, collecting the condensed tar at the bottom of the shell body of the drawer-type oil. This utility model use the dividing wall water-cooling heat exchanger, the cooling water pipe is bent into curved shape is fixed on the steel plate, the structure improves the cooling effect, the tar separating better, and can use the heat energy in the biomass gasification gas heating cold water in the water pipe, improves the heat efficiency, and has simple structure, low manufacturing cost, easy to clean, easy to replace, the practicability is stronger.
NOVELTY - This utility model claims a kind of energy saving biomass gasification boiler, comprising a water jacket furnace body, water jacket is connected with a water pipe fire grate in the water jacket furnace body, the ash chamber, a combustion chamber and a gasification chamber of water pipe fire grate is set on the water jacket of the furnace body in the lower part, the lower part is water pipe fire grate is an ash chamber, a water pipe fire grate is a combustion chamber and a gasification chamber, a gasification chamber on the two sides of the combustion chamber, the upper part is a gasification chamber is set with feed inlet and sealing cover, combustion chamber, the upper part of the space is provided with multiple communicated water jacket heat absorption water pipe, upper part of the combustion chamber is provided with a water sleeve type heat exchanger, a sleeve type heat exchanger is provided with multiple communicated water jacket heat absorption water pipe, a water sleeve type heat exchanger smoke outlet is set on the upper part, the lower part of the combustion chamber is provided with multiple connected two sides of the gasification chamber of the gas through hole. It has simple structure, is convenient to use, burn adequately, thermal efficiency is high.
NOVELTY - Fermented biological organic fertilizer comprises 56.5-57.5 pts. wt. Agaricus bisporus waste, 9-11 pts. wt. perlite, 9-11 pts. wt. silica, 0.4-0.6 pts. wt. water retention agent, 14-16 pts. wt. sawdust, and 4-6 pts. wt. slow release fertilizer.    USE - As fermented biological organic fertilizer (claimed) for vegetable, flower, economic crop, and tobacco.    ADVANTAGE - The fermented biological organic fertilizer is easily absorbed by crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing ferment biological organic fertilizer involves drying waste Agaricus bisporus at more than 10 degrees C to reach the water content of 28-30%; putting into a crusher to crush, where the grain diameter is less than 15; sieving to remove large particle diameter material; then proportioning adding silica, perlite, water retention agent, slow release fertilizer, sawdust into the mixer to mix them for 3 minutes to obtain the product.
NOVELTY - Producing clodinafop-propargyl microemulsion involves adding raw material formulation comprising 12-18 pts. wt.% clodinafop-propargyl solvent, 22-28 pts. wt.% latent solvent, 15-10 pts. wt.% surface active agent, and water in stirring tank, stirring at normal temperature, stirring for 1.5-2 hours, adding the prescription amount of water added in second stirring tank, and adding prescription amount of surface active agent, stirring till completely dissolving the surface active agent into high speed stirring tank at normal temperature.    USE - For producing clodinafop-propargyl microemulsion (claimed).    ADVANTAGE - The method has simple technique, mild reaction condition, no pollution waste discharge and good product quality; improves the pesticide active ingredient clodinafop-propargyl dispersion uniformity, and improves the utilization rate of the preventing and treating effect and medicament.    DETAILED DESCRIPTION - Producing clodinafop-propargyl microemulsion, where the raw material formulation comprises 12-18 pts. wt.% clodinafop-propargyl solvent, 22-28 pts. wt.% latent solvent, 15-10 pts. wt.% surface active agent, and the rest is water, involves stirring tank, adding solvent formulation, stirring at normal temperature, rotating speed of the stirrer is 50-80 revolution/minutes, stirring and in turn adding latent solvent of formula amount, clodinafop-propargyl, stirring for 1.5-2 hours, adding the prescription amount of water added in the second stirring tank, stirring at normal temperature, rotating speed of the stirrer is 40-60 revolution/minutes, stirring and adding prescription amount of surface active agent, stirring till completely dissolving the surface active agent into the high speed stirring tank at normal temperature, high speed stirring tank, a stirrer rotating speed is 210-220 revolution/minutes, to obtain the surface active agent water solution into high speed stirring tank, stirring for 1.2-1.5 hours to obtain finished product.
NOVELTY - Invention relates to chemistry. Apparatus for producing hydrogen from water consists of a housing in which there is a reactor, where electrodes are mounted while applying voltage across said electrodes, the apparatus being characterised by that working electrodes are in form of mesh cylinders made from aluminium alloys, inserted into each other with a spacing to form a bundle, wherein an atomiser is inserted from the bottom of the bundle, the atomiser being connected to a high pressure pump which is connected to a heating vessel mounted at the exhaust manifold of a car, which along with the bundle is connected to a source of intermitted high voltage, and the bundle of mesh cylinder electrodes is mounted in a high-voltage acceleration electric field between electrodes connected to a source of a high-voltage field.    USE - Chemistry.    ADVANTAGE - Low cost of producing hydrogen and high efficiency.
NOVELTY - The manufacturing method involves substituting gas in the space of container (3) with a first gas same as the fuel such as hydrogen, second gas of the same oxide of the fuel, or mixed gas which is a mixture of the first gas and second gas. The number of the molecules of the gas in the space is adjusted to a number with which the entire pressure of the gas in the space becomes smaller than atmospheric pressure when the space is at room temperature. The valves (5,7) and space are closed after the substitution process.    USE - Manufacturing method of fuel cell system.    ADVANTAGE - Improves durability without sacrificing electric power generation efficiency by suppressing pressure difference between interior and exterior inside of a closed space and the exterior of fuel production component, from becoming large during operation of fuel cell part.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell system. (Drawing includes non-English language text).    Fuel production component (1)    Fuel cell part (2)    Fuel electrode (2B)    Container (3)    Valves (5,7)
NOVELTY - The method involves producing an open-pored and fluid-permeable support material (122) i.e. oxide forming material, which includes pores (124) forming a cavity (126) in the support material. A protection layer (130) is produced at an inner surface (128) of the support material by superficial oxidation of the support material, where the inner surface defines the cavity. An electron-conductive structure (134) extending within the cavity of the support material is produced. The electron-conductive structure is formed from a ceramic material.    USE - Method for manufacturing a support substrate i.e. metal substrate, for a high temperature electrolyte layer i.e. ceramic yttrium oxide-stabilized zirconium-dioxide layer, for an electrochemical device such as a high-temperature fuel cell device (all claimed) i.e. solid oxide fuel cell.    ADVANTAGE - The electron-conductive structure extending within the cavity of the support material is produced, thus manufacturing the stable and easily stackable support substrate with a high electron conductivity, and hence efficiently operating the high-temperature fuel cell device with reduced loss. The utilization of the protection layer reduces thermal and/or chemical loads of the support material during operation of the electrochemical device. The method avoids occurrence of mechanical stresses within the support substrate in high temperatures.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a support substrate    (2) an electrochemical device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a support substrate for a high temperature electrolyte layer of a high-temperature fuel cell device.    Open-pored and fluid-permeable support material (122)    Pores (124)    Cavity (126)    Inner surface of an open-pored and fluid-permeable support material (128)    Protection layer (130)    Electron-conductive structure (134)
NOVELTY - This utility model claims a kind of regeneration processing system of construct waste, comprising a dry-wet separation of dry-wet separation device for waste, for carrying out the crushing sorting the solid garbage is rough sorting device for the garbage to the crush again refining crushing sorting of the sorting crushing device used for re-refining the crushed garbage to synthetic regenerative connected with synthetic regenerative device of organic fertilizer, and the inlet is used for controlling the device of the central processing unit, wherein the dry-wet separation device is connected with the rough sorting device, the rough sorting device is connected with the sorting crushing device is connected with the inlet of the synthetic regenerative device of the sorting crushing device is connected with the central processor respectively connected with the dry-wet separation device, sorting device and a sorting crushing device, regenerative device are electrically connected. The beneficial effect of the utility model is as follows: a. re-pollution discharge device of full-automatic, which really realizes the digestion of environment-friendly requirements of the domestic garbage from the source.
NOVELTY - The method involves closing a natural gas steel bottle valve. A natural gas steel bottle valve port is matched with a pipeline. A multi-stage reciprocating compressed natural gas compressing device is connected with the pipeline. A qualified natural gas steel bottle is filled with nitrogen gas. A detection mark is fixed on the qualified natural gas steel bottle. A summarizing test recording parameters are collected. An issuing detection report file is contained with a detection report. A withdrawing station is fixed with a qualified natural gas steel bottle according to the detection report.    USE - Method for detecting residual gas in a natural nitrogen gas-liquid steel bottle.    ADVANTAGE - The method enables detecting residual gas and liquid in a natural nitrogen gas-liquid steel bottle, reducing gas resources wastage rate and preventing environment from being polluted.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for detecting residual gas in a natural nitrogen gas-liquid steel bottle.'(Drawing includes non-English language text)'
NOVELTY - Use of blue-green algae and straw agricultural wastes is claimed as raw material for producing Agaricus bisporus culture medium.    USE - The blue-green algae and straw agricultural wastes is used as raw material for producing A.bisporus culture medium (claimed).    ADVANTAGE - The blue-green algae and straw agricultural waste enables producing high-quality culture medium for the A.bisporus. The raw materials increase production of the culture medium by 10-15% and reduce cost of compost raw material by 50% or more. The method effectively increases utilization rate of the blue-green algae and straw that are often discarded as waste (effective utilization of waste as beneficial product), hence environmentally-friendly and provides high social and economic benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing culture medium of A.bisporus, which involves using combination of blue-green algae and straw, as raw materials.
NOVELTY - The system has a fermenting tank (1) that is connected with a farm. A solid-liquid separating device (2) is connected with the fermenting tank that is connected with a filtering device (3). The filtering device is connected with the solid-liquid separating device. A pump station (4) is respectively connected with the filtering device and farmland of outside through pipeline.    USE - Field animal excrement processing system.    ADVANTAGE - The occupied land of culturing farm can be saved, and environment surrounding the culturing farm can be protected. The harmful substances such as heavy metals can be filtered from the animal feces, so that the animal feces are changed into safe organic fertilizer. The waste reclamation can be realized, soil can be improved, and farmland can be protected. Economic and social benefits of the culturing farm can be greatly increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the field animal excrement processing and utilization system. (Drawing includes non-English language text)    Fermenting tank (1)    Solid-liquid separating device (2)    Filtering device (3)    Pump station (4)    Three-way valve (5)
NOVELTY - Preparing 4-androstenedione involves: collecting mycelium and slag in plant phytosterin fermentation liquid using plate-and-frame filter press or centrifuge disc; extracting 4-androstene diketone crude product (I) by combining the mycelium and slag with acetone; and preparation of pure 4-androstenedione by dissolving the crude product (I) in acetone water solution, filtering, cooling and centrifuging to obtain the product (II), followed by dissolving the product (II) in ethanol, adding active carbon, stirring, filtering and washing the crystal with cold ethanol.    USE - For preparing 4-androstenedione (claimed).    ADVANTAGE - The method is simple, shows good extracting effect, provides highly pure 4-androstenedione, recycles the non-transformed plant sterol, reduces the environment pollution, and is economical and suitable for industrial production.    DETAILED DESCRIPTION - Preparing 4-androstenedione from plant phytosterin ferment liquid involves: (1) collecting mycelium and slag in plant phytosterin fermentation liquid using plate-and-frame filter press or centrifuge disc; (2) extracting 4-androstene diketone crude product (I): combining the mycelium and slag with acetone at normal temperature, centrifuging and collecting the filtrate and un-reacted phytosterin, concentrating the filtrate, decompressing, evaporating and recycling acetone, and crystallizing to obtain the 4-androstene diketone crude product (I); and (3) preparation of pure 4-androstenedione involving: dissolving the crude product (I) in acetone water solution by refluxing, filtering, cooling the filtrate to 4 degrees C for 3hours, centrifuging and collecting the product (II), dissolving the product (II) in ethanol and refluxing, adding active carbon followed by stirring and de-coloring for 30 minutes, followed by filtering, cooling, and centrifuging, and washing the crystal with cold ethanol and drying for 5-8 hours.
NOVELTY - Producing biogas from lignocellulose containing raw material comprises (i) adding cellulase solution (3-10 mg/g of raw material) to the lignocellulose containing raw material, adding 5-13 times of water according to the dry weight of the raw material, processing for 1-48 hours at 35-50 degrees C to obtain the preprocessed raw material; and (ii) subjecting the preprocessed raw material to anaerobic fermentation in a biogas tank to obtain the biogas.    USE - The method is useful for producing biogas from lignocellulose containing raw material (claimed).    ADVANTAGE - The method: improves the biogas yield (claimed), ensures the degradation of degradation-resistant cellulose substances by using cellulase solution, improves the substrate utilization rate, and solves the problem of floating of raw materials on the biogas slurry.
NOVELTY - The plant yield increasing device has upper cover (1) whose lower surface edge is provided with air outlet hole (21) at height of 40-50 mm. The gas head (3) is formed on the casing (2). The area of gas outlet is formed in the range of 870-1750 mm2. The area of the air proportioning port is set to 428-858 mm2. The air inlet is matched with the gas source outlet of the air source. The diameter of the air inlet is set to 2.0-2.2mm, if the air source is marsh gas. The diameter of the air inlet is set to 0.9mm, if the air source is natural gas or liquefied gas.    USE - Plant yield increasing device.    ADVANTAGE - The yield of the plant can be increased with minimum resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant yield increasing device.    Upper cover (1)    Casing (2)    Gas head (3)    Arc-shaped structure (12)    Air outlet hole (21)
NOVELTY - This utility model claims a kind of amino acid fermentation system culture base material liquid recycling device, to which a material liquid, material liquid recycling tank, recycling pipe, the material liquid recycling main pipe and a material recovery tank, a liquid recycling groove is set on the sampling opening, a liquid recovery device upper part inlet with the fermentation tank exhaust pipe is connected with the lower part of the material liquid recycling pipeline connected with the material liquid recycling pipeline through a material liquid recycling pipe and material recovery tank. Utilizing and recycling device for recycling the amino acid fermentation system generated in the process of waste material liquid culture medium, and collecting the material recovery tank to store and for later batch fermentation material passes through; The recovery process is easy to realize, it can improve the production utilization rate of raw material, effectively saves the production cost.
NOVELTY - This utility model claims a kind of message fermentation industry water recycling device, comprising a fermentation tank (1), a collecting pipe and a condenser (3), a fermentation tank (1) and recycling pipe (6) is connected with the fermentation tank (1) through the collecting pipeline (2), a condenser (3) and water storage tank (5) is connected with a collecting water of the fermentation culture medium in the fermentation process to replace water recycling fermentation culture medium is adjusted, is used for fermenting and producing glutamic acid. The utility model is provided with water-saving, environmental protection and so on, it can be widely applied to fermentation, chemical industry, food, it has very good popularization and application value.
NOVELTY - This utility model claims a biomass gasification furnace hearth material on feeding control device, comprising a material level sensing rod (8) and a sensor (7), the material level sensing one end of the supporting rod (8) is a detecting plate (11), the hearth (2), a gas outlet (10), a sensing rod (8) rod body passes through the hearth (2) and the hearth (2) is connected, a sensing rod (8), one end of the lower part is provided with a material level sensor (7). Material position sensing rod (8) and the hearth (2) is set on the pivot to form lever. Material position sensing rod (8) passes through sealing piece (9) is connected with the 2 on the wall of the hearth. A material swinging process of the sensing rod is material position control process, a material level sensor senses said position detecting plate and the feeding control process, the utility model is a material feeding and accurate control, the control device itself is flexible and durable.
NOVELTY - The cell (100) has separator (2) that divides space inside housing (1) into spaces (3,4). A counter electrode (7) and optical semiconductor electrode (6) are arranged in respective spaces. An electrical connection component (8) is positioned to electrically connect between optical semiconductor electrode and counter electrode. An electrolyte solution supply hole (10) is positioned rather than electrolyte solution discharge hole (11) at perpendicular upper side. The water is decomposed and hydrogen is generated by irradiating light to optical semiconductor electrode.    USE - Hydrogen generation cell of hydrogen generation device for energy system (all claimed).    ADVANTAGE - The hydrogen generation efficiency of the hydrogen generation cell can be improved. The structure of the hydrogen generation cell can be simplified so that the space-saving can be attained efficiently. Multiple hydrogen generation cells can be connected simply and rationally. The practical use degree of the hydrogen generation cell can be improved. The piping length and the number of manifolds can be reduced significantly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a hydrogen generation device; and    (2) an energy system.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the hydrogen generation cell.    Housing (1)    Separator (2)    Spaces (3,4)    Conductive substrate (5)    Optical semiconductor electrode (6)    Counter electrode (7)    Electrical connection component (8)    Electrolyte solution supply hole (10)    Electrolyte solution discharge hole (11)    Hydrogen generation cell (100)
NOVELTY - A lily bulb producing method involves preparing explant by cutting lily squama into small blocks, sterilizing and inoculating in a solid culture medium, performing proliferation culturing by using intermittently immerging tissues and organs of plant bioreactor to culture, and performing intermittent immersion at illumination intensity of 1500-1800 lux for 14 hours/day at culture temperature of 22-28 degrees C for 25-80 days to obtain finished product.    USE - Method for producing lily bulb.    ADVANTAGE - The method enables producing lily bulb in an inexpensive and eco-friendly manner.
NOVELTY - The garbage disposal device has a garbage degradation chamber (1) that includes a first air inlet and a first air outlet. A pressurizing chamber is connected with the garbage degradation chamber, to compress garbage degradation chamber. The dust-removing sterilizing elements are arranged inside a sterilizing tower (4). The sterilizing tower is provided with a second air inlet and a second air outlet. A de-sulfurizing tower (5) is provided with a third air inlet and a third air outlet. The third air inlet and second air outlet are connected with an air storage tank (6).    USE - Garbage disposal device.    ADVANTAGE - The reusable effect of the garbage can be improved efficiently while effective environment protection can be ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the garbage disposal device.    Garbage degradation chamber (1)    Heating chamber (2)    Sterilizing tower (4)    De-sulfurizing tower (5)    Air storage tank (6)
NOVELTY - Compressed air connection blasting method involves introducing steam to the loading of a crock material to a desired pressure value, the pressure valve for compressed air crock, pressure blasting pressure value and the compressed air valve and pressure for a period of time exploded material.    USE - As compressed air connection blasting method (claimed), used for pre-processing the household garbage, the garbage in the fat, protein, lignin, cellulose.    ADVANTAGE - The method reduces steam energy consumption based on keeping the blasting effect, reduces the blasting processing method of steam pressure, effectively breaks through the processing station is difficult to obtain high pressure steam of the bottle neck, improves blasting efficiency, it has better overall performance.
NOVELTY - Preparing biological sludge conditioner involves preparing seed liquid: freezing Bacillus licheniformis p-104 strain having preservation number of CGMCC No. 4156 and inoculating into seed culture medium, culturing for 8-14 hours; and fermenting culture: inoculating 1-5% the seed solution in the fermentation culture medium, and fermenting at pH of 5-9, temperature of 30-37 degrees C, and 150-200 rotation per minute for 30-36 hours, and collecting fermentation liquid sludge conditioning agent.    USE - For preparing biological sludge conditioner useful in sewage treatment (claimed).    ADVANTAGE - The method prepares biological sludge conditioner that has greatly improved sludge dehydration efficiency, is environment-friendly and biodegradable, and does not generate secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge conditioning involving taking active sludge; adjusting pH to 5-9; taking 0.003-0.04 vol.% the sludge conditioning agent; and stirring the mixture at 220 rotation per minute for 1 minute, then 80 rotation per minute for 30 s, and standing for greater than or equal to 5 minutes.
NOVELTY - Compression-type forest tree seed cultivating substrate is obtained by preparing compression block by blending 10-20 wt.% sandy soil, 75-85 wt.% decomposed forestry and agricultural residues and 0.1-5 wt.% peach gum.    USE - The compression-type forest tree seed cultivating substrate is used in nursery stock enterprises and forestation enterprises in batch for large-scale forest tree propagation.    ADVANTAGE - The substrate increases germination rate of tree seeds and strengthens seedlings, and can also be sold on the market and cultivated in a household by an individual person. The substrate is low in cost and capable of achieving the effects of sufficiently utilizing a great number of cheap forestry and agricultural residues, thus provides economic benefits and environmental benefits. The cultivated nursery stock can also be transplanted outdoors, so that the environment is indirectly protected.
NOVELTY - Extracting lignin from lignocellulosic biomass comprises pre-processing biomass raw material using organic acid solution including a formic acid with a concentration of 30-90% and acetic acid with a concentration of 5-50%, reacting, controlling temperature to 70-165 degrees C for 10-150 minutes, separating solid-liquid phase to obtain reaction liquid at 60-100 degrees C and 0.06-0.1 atmospheric pressure, decompressing and distilling, concentrating, adding auxiliary agent, reacting at 60-70 degrees C, carrying out solid-liquid separation to obtain solid, esterifying, stirring and washing using water.    USE - The method is useful for extracting lignin from lignocellulosic biomass (claimed).    ADVANTAGE - The method extracts lignin with high extraction rate of 85% and low energy consumption in a simple manner.
NOVELTY - Manufacture of arabinose involves providing cellulosic biomass, hydrolyzing to obtain hydrolyzate, performing neutralization, desalting, optional concentration and membrane filtration on the obtained hydrolyzate and obtaining monosaccharide solution portion and non-monosaccharide solution portion, fermenting obtained monosaccharide solution portion and obtaining fermentation broth, distilling fermentation broth to obtain ethanol byproduct and arabinose solution portion, refining, obtaining arabinose product, adsorbing obtained non-monosaccharide solution portion.    USE - Manufacture of arabinose and its by-products e.g. ethyl alcohol, xylo-oligosaccharide, plant polyphenols, and plant flavonoids.    DETAILED DESCRIPTION - Manufacture of arabinose with byproducts, which involves providing cellulosic biomass, hydrolyzing the cellulosic biomass and removing components excluding cellulose and lignin to obtain hydrolyzate, performing neutralization, desalting, optional concentration and membrane filtration on the obtained hydrolyzate and obtaining a monosaccharide solution portion and a non-monosaccharide solution portion which are separated, fermenting the obtained monosaccharide solution portion and obtaining fermentation broth, distilling the fermentation broth to obtain an ethanol byproduct and an arabinose solution portion which are separated, and refining the arabinose solution portion and obtaining arabinose product, adsorbing the obtained non-monosaccharide solution portion by using resin to obtain plant polyphenol and a plant flavonoids byproduct, and an oligosaccharide solution, which are separated. An INDEPENDENT CLAIM is included for usage method of cellulosic biomass for preparing arabinose and its by-products.
NOVELTY - A kind of a particle cleaning technology of plate-type membrane biochemical reactor, relating to a sewage treatment device, it comprises the particles (1), a frame (2), a flat plate ultra-filtration membrane (3), the micro-porous aeration pipe (4) and a tank (5), a pool (5) is set with a component frame (2), a frame (2) is uniformly provided with multiple of panel ultrafiltration membrane (3), and the film assembly frame (2) inner side and outer side of the suspension is distributed with several of the particles (1), ultra-filtration membrane (3) is uniformly provided with multiple of micro-pore aeration pipe (4). It has simple structure, low cost, can automatically clean internal membrane device, and the cleaning effect is good, it is convenient to use.
NOVELTY - A kind of constant temperature stirring vertical marsh gas pool, comprising a tank body shell, a waterproof layer, a feeding port, a thermometer, a stirrer, an air guide pipe, a cartridge and a gas storage device, a spacing and a constant temperature control device. The tank body shell is the main body supporting part is a alkali-free platinum glass fibre winding mechanism is made of high strength. Heat preservation is provided with waterproof layer is set on the outer surface of the tank body shell, the upper part of the tank body shell is provided with a feeding port is further provided with a toilet urinal connected to the feeding port on the pipe. A feeding end adjacent, provided with provided with temperature meter. Provided with a stirrer and a gas-guide tube on the tank body middle part. The guide tube is provided with a cartridge, a gas-guide tube is connected with the gas storage device. Pool body middle part is provided with a pipe with external water pressure region connected with. Winding is provided with a constant temperature control device is set on the tank body shell middle part inner wall of the constant temperature control device is connected with an external cold and hot source. This utility model has simple structure, convenient installation and use, high temperature resistance, corrosion resistance, aging resistance and long service life.
NOVELTY - A kind of constant temperature stirring Horizontal methane pool, comprising a pool body shell, heat preservation waterproof layer, a feeding port, a thermometer, a stirrer, an air guide pipe, a cartridge and a gas storage device, a discharge port, a constant temperature control device and the inner reinforcing rib. The tank body shell is the main body supporting part is a alkali-free platinum glass fibre winding mechanism is made of high strength. Heat preservation is provided with waterproof layer is set on the outer surface of the tank body shell, the upper part of the tank body shell is provided with a feeding port is further provided with a toilet urinal connected to the feeding port on the pipe. A feeding opening, is provided with a temperature meter, a monitoring of temperature change. Provided with a stirrer and a gas-guide tube on the tank body middle part. The guide tube is provided with a cartridge, a gas-guide tube is connected with the gas storage device. Is provided with a discharging port on the corresponding other side is connected with the feeding port. The tank body middle part on the inner wall is provided with an inner reinforcing rib for increasing the tank body. This utility model has simple structure, convenient installation and use, high temperature resistance, corrosion resistance, aging resistance and long service life.
NOVELTY - Anti-pollution injector belongs to the technical field of medical appliance. The technical solution is as follows: the utility model comprises a needle head, a needle tube, a piston and a needle core, wherein it is provided with an elastic sterile cover the front section of the needle tube, the elastic sterile cover is provided with a " C "-shaped groove, and the " C "-shaped sterilizing groove is provided with a sliding arm, the front end is provided with a sterilizing clamp. This utility model has simple structure, when the patient is injected can completely prevent the injection site infection and reduce the working difficulty of the medical staff.
NOVELTY - This utility model claims a baffle adhering membrane type methane tank, removing the unnecessary pool body, feeding port, discharging port and a biogas outlet, further comprising a tank body arranged air outlet baffle plate, said baffle plate can be detached and installed, and with adhesive film. This utility model claims a baffle adhering membrane type methane tank, which is formed by the combination of the baffled marsh gas tank and adhering membrane type methane tank, the baffle does not need to stir, the energy consumption is low, the operation is convenient and the efficiency is high, the film can bear load change, and the baffle plate pressing adhesive film (for attached gas ferment bacteria) is in the form of a movable, it not only is convenient to install, but also reduces the baffle plate volume. Baffle, adhering membrane type biogas tank is set with adhesive film with the baffle plate, the fermentation material enters from the feeding port, flowing along the baffle plate up and down, the process flow according to the order of the fermentation bacteria on the adhesive film, digestion, release the methane gas.
NOVELTY - Improving water quality stored in antifluctuating zone, comprises trimming terraced plots, inclining the slope, forming reverse slope between upper and lower retaining construction walls, digging ditches at bottom part of the slope, carrying out annual seedling to mulberry plant, transplanting, planting large and small sub-classification seedlings in edge, cutting stems, transplanting bermuda grass, and harvesting the plant and grass at different growth stages by bio-gas fermentation method.    USE - The method is useful for improving quality of water in antifluctuating zone by planting plants, which are used as a feed for a livestock (claimed).    ADVANTAGE - The method ensures improved water quality by planting plants in sidewalls of zone to absorb nitrogen, phosphorus and soil pollutants in antifluctuating zone to prevent water from being polluted.    DETAILED DESCRIPTION - Improving water quality stored in antifluctuating zone, comprises trimming terraced plots, slightly and inwardly inclining the slope to 3-5 degrees , forming reverse slope between upper and lower retaining construction walls, longitudinaly digging ditches at bottom part of the slope in a foot protection and riprap protection zones having height of 2 m, carrying out annual seedling to mulberry plant, transplanting large and small sub-classification seedlings in a row spacing of 100x 30 cm, cutting stems into 15-20 cm of long segments, where the stems are planted in a 10-15 cm of groove with spacing of 30-40 cm, preferably 15-20 cm, transplanting Bermuda grass 20-30 cm of spacing 40x 40 cm, and harvesting the plant and grass at different growth stages by bio-gas fermentation method.
NOVELTY - The processor has a fermentation trough that is connected with discharge hole of grinding and dewatering system. The discharge opening (17) is positioned on lower portion of right side of processor portion (18). The heating system is arranged at the bottom of the fermentation trough. A heater is arranged in the heating system. The liquid waste collecting system is provided with water tank positioned below fermentation trough. The tail end of water tank is provided with oil discharge valve (16) and water discharge valve (15).    USE - Kitchen waste microbe processor.    ADVANTAGE - The kitchen waste microbe processor, grinding and dewatering pretreatment can be performed on the kitchen waste, so that adverse effect on the microbe treatment caused by much moisture and high oil content is eliminated. The material mixing efficiency is enhanced by adopting the fermentation trough. The processing efficiency of kitchen waste is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the kitchen waste microbe processor.    Electric control box (5)    Water discharge valve (15)    Oil discharge valve (16)    Discharge opening (17)    Processor portion (18)
NOVELTY - Selenium-enriched organic fertilizer is prepared by mixing and uniformly stirring 5-10 pts. wt. silkworm excrement, 10-80 pts. wt. chicken manure, 1-5 pts. wt. molasses water, and 1-3 pts. wt. 80 meshes bentonite, inoculating 0.6-1.6 pts. wt. liquid microbial strain, performing micro-aerobic constant-temperature fermentation at 32 degrees C for 48 hours, adding 0.1-0.39 pts. wt. powdery trace elements, and performing granulation, low-temperature drying or air drying to reach humidity of 12% to obtain the fertilizer.    USE - As selenium-enriched organic fertilizer (claimed).    ADVANTAGE - The fertilizer is rich in antibacterial peptide flora, humic acid, enzymes, vitamins, exopolysaccharides, selenium and crop growth promoting factors, can optimize soil environment, improves immunity, crop nutrition absorptivity and fertilizer utilization rates, increases selenium content of crops, is an optimum selection for the development of high quality agriculture in our country, and is suitable for large-area popularization and application.
NOVELTY - A fuel cell power generation system comprises reforming reactor provided with sulfur compound-resistant modification catalyst introduced without desulfurizing sulfur compound-containing hydrocarbon gas for hydrogen generation and fuel cell (5) into which hydrogen-containing gas from reforming reactor is introduced. Sulfur compound-resistant modification catalyst contains barium titanate and/or strontium titanate.    USE - A fuel cell power generation system (claimed).    ADVANTAGE - Poisoning with sulfur compound is prevented, hydrogen generation efficiency is improved, the need to use expensive noble metal catalyst is eliminated, size of desulfurizer in fuel cell power generation system is reduced, structure of fuel cell power generation system is simplified, and power cost is lowered.    DESCRIPTION OF DRAWING(S) - The drawings show block diagrams of fuel cell power generation systems. (Drawing includes non-English language text).    Desulfurizer (1)    Modifier (2)    CO modifying device (3)    CO selective oxidation device (4)    Fuel cell (5)
NOVELTY - This utility model claims a piggery external zero discharge fermenting bed, comprising: means for making a piggery to the fermentation product conveying fermenting bed material out of the conveying platform and receiving conveying platform transmitted the fermentation bed is provided on the outside of a house, the utility model is convenient to operate, use electric automatic control over a target computer, the target turning rate, separating the fermenting bed piggery and, according to a normal condition, reduces the risk of stress pig disease control, at the same time by uniformly spraying pump and target machine back and forth process, which can improve the treatment effect of the fermentation bed.
NOVELTY - Oral mucosa sustained-release pharmaceutical composition comprises oral mucosa contact layer and non-adhesive sealed layer. The oral mucosa contact layer comprises components of antibiotic medicine and auxiliary material in the weight ratio of 2-20:80-98 and non-adhesive sealed layer comprises components of non-adhesive low water soluble high molecular polymer which is chosen from polyvinyl alcohol. The composition comprises 4 g chlorhexidine, 12 g hydroxyethyl cellulose, 5.5 g modified starch, 7 g microcrystalline cellulose, 0.5 g grape essence and remainder polyvinyl alcohol.    USE - The oral mucosa sustained-release pharmaceutical composition is useful for treating oral and periodontal diseases (claimed).    ADVANTAGE - The oral mucosa sustained-release pharmaceutical composition rapidly releases drug for long time, is convenient for delivering drugs, specific with respect to target, and has strong mucosa adhesive force. The method is simple to operate, cost-effective, environmentally-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Oral mucosa sustained-release pharmaceutical composition comprises oral mucosa contact layer with 0.5-2 mm thickness and non-adhesive sealed layer with 10-50 mu m thickness. The oral mucosa contact layer comprises components of antibiotic medicine and auxiliary material in the weight ratio of 2-20:80-98 and non-adhesive sealed layer comprises components of non-adhesive low water soluble high molecular polymer which is chosen from polyvinyl alcohol. The composition comprises 4 g chlorhexidine, 12 g hydroxyethyl cellulose, 5.5 g modified starch, 7 g microcrystalline cellulose, 0.5 g grape essence and remainder polyvinyl alcohol.
NOVELTY - The apparatus (1) has modifier (10) that reforms a mixed gas of raw material and water vapor. A combustor (2) heats the modifier by burning a combustible gas. A hydrodesulfurization device (14) is provided such that heat is supplied from the modifier and removes sulfur in the raw material to be supplied to modifier by reacting sulfur with hydrogen. A heat insulating material (13) is arranged between the hydrodesulfurization device and the modifier. Uniform-heating board (18) is arranged between the hydrodesulfurization device and the heat insulating material.    USE - Hydrogen generating apparatus used for generating fuel gas, for fuel cell power generating device. Can also be used in natural gas, liquified petroleum gas, petrol, kerosene, methane, ethane, propane, butane, pentane and another hydrocarbon.    ADVANTAGE - Since temperature difference arises in the upper portion and the lower portion of hydrodesulfurization device can be moderated by the heat conduction of uniform-heating board, the temperature of the whole hydrodesulfurization device can be equalized. The temperature of the whole hydrodesulfurization device can be optimized. Small and low-cost hydrogen generating apparatus can be obtained with simple structure. The hydrogen generating apparatus can minimize the amount of mounting of desulfurization catalyst. Since hydrogen generating apparatus can make the temperature distribution of the whole hydrodesulfurization agent small, the usage-amount of the hydrodesulfurization agent is restrained at worst.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Combustor (2)    Modifier (10)    Heat insulating material (13)    Hydrodesulfurization device (14)    Uniform-heating board (18)
NOVELTY - The method involves treating a wastewater in a mainstream, separating primary sludge from the wastewater and producing a primary effluent. The wastewater in the mainstream reactor is treated to remove carbon and a secondary effluent. The primary sludge and secondary sludge are treated in a side stream. The secondary effluent in the mainstream is contacted with the biomass to reduce the ammonium concentration in the secondary effluent. The biomass is rejuvenated by contacting the biomass with the reject water. Ammonium is removed from the secondary effluent in the mainstream by deammonification biofilm reactor.    USE - Method for biologically treating wastewater in wastewater treatment system to remove carbon and ammonium.    ADVANTAGE - The exposure of the biomass to the wastewater in the side stream having the relatively high ammonium concentration is effective to rejuvenate the anaerobic ammonium oxidizing (ANAMMOX) bacteria such that when the ANAMMOX bacteria is brought back into contact with the wastewater in the mainstream. The ANAMMOX bacteria are effective to reduce the ammonium concentration of the wastewater in the mainstream.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a mainstream and side stream process for treating wastewater and removing carbon and ammonium from the wastewater;    (2) an integrated fixed film activated sludge system wastewater treatment method for reducing concentration of ammonium in wastewater; and    (3) an integrated fixed film activated sludge process for removing ammonium from wastewater in mainstream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the de-ammonification process.    Primary clarifier (54)    Biological treatment reactor (58)    Secondary effluent line (60)    Sludge thickener (80)    Bio film transfer devices (90,92)
NOVELTY - The utility model claims a fluidized bed device comprises large granule urea ammonia tail-gas treating system, solves the problem that the existing fluidized bed large granule urea tail gas of phenol-acetone device processing system is provided with dust removing effect and does not have ammonia; A solution comprises a dust washing tower, further comprising a removing ammonia absorption tower, wherein the ammonia removing absorption tower is provided with a water inlet, a tail gas inlet and a tail gas outlet, ammonium sulphate solution outlet and a solution circulation inlet, the dust washing tower tail gas outlet through the pipeline is connected with the tail gas inlet of the ammonia absorbing tower, is connected with a draught fan and a tail gas outlet through the pipeline of the ammonia absorption tower, ammonium sulphate solution outlet is connected by a solution circulating pump is connected with the circulating solution; This utility model has simple structure, is easy to control, the equipment investment is low, the operation cost is low, at the same time recycling a urea dust in the tail gas and ammonia.
NOVELTY - A Bacillus subtilis strain S001 (CGMCC 6425), is new.    USE - The B.subtilis strain S001 is useful for inhibiting several pathogens including Fusarium, and Rhizoctonia solani, tomato leaf mold, tomato early blight pathogen, tomato grey mold, wheat root rotting pathogen and wheat sheath blight pathogen, and preparing pesticides and fertilizers (all claimed).    ADVANTAGE - The fertilizer prepared using the above-mentioned strain is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microbial preparation, which is prepared using the above-mentioned B.subtilis strain S001.
NOVELTY - Method for composting seaweed residue involves (a) drying fresh seaweed residue, until the water content reaches 50-55%, (b) piling the seaweed residues into stack and taking initial sample and recording initial temperature, measuring bulk density, porosity, water content, pH, electrical conductivity (EC) value, organic carbon content and germination index, (c) covering the stack using plastic film for preserving heat, and (d) overturning the stack once every 3 days depending upon the environmental condition and sampling the above-mentioned parameters for complete composting.    USE - The method is useful for composting seaweed residue, which is used as vegetable seedling matrix (claimed).    ADVANTAGE - The method is simple as the need for adding nitrogen fertilizer is eliminated by maintaining carbon and nitrogen ratio, so mechanical stack overturning is made easy, and shortens the fermentation time by controlling water content and temperature accurately.
NOVELTY - A paste fertilizer is prepared by mixing chicken manure powder, weathered coal, corn flour, and wheat bran to obtain first mixture; mixing potato, corn flour, wheat bran, and water, boiling, and uniformly stirring to obtain second mixture; dissolving ammonium bicarbonate, calcium superphosphate, potassium humate, fulvic acid, brown sugar, amino acid powder, and trace element in water, pouring second mixture, and adding fermenting agent to obtain third mixture; uniformly mixing with first mixture, sealing, and fermenting; and adding mixture of amino acid powder and yeast powder and stirring.    USE - Method for preparing paste fertilizer (claimed).    ADVANTAGE - The fertilizer is environment-friendly and has low cost.    DETAILED DESCRIPTION - A paste fertilizer is prepared by mixing 800-1000 pts. wt. chicken manure powder, 65-85 pts. wt. weathered coal, 7-9 pts. wt. corn flour, and 8-10 pts. wt. wheat bran to obtain first mixture; mixing 0.5-1.5 pts. wt. potato, 1.5-2.5 pts. wt. corn flour, 0.5-1.5 pts. wt. wheat bran, and 15-25 pts. wt. water, boiling, and uniformly stirring to obtain second mixture; dissolving 7-9 pts. wt. ammonium bicarbonate, 2.5-4 pts. wt. calcium superphosphate, 12-20 pts. wt. potassium humate, 1.5- 2.5 pts. wt. fulvic acid, 0.3-0.7 pts. wt. brown sugar, 8-12 pts. wt. amino acid powder, and 0.08-0.16 pts. wt. trace element in 350- 450 pts. wt. water, pouring second mixture, and adding 4.5-5.5 pts. wt. fermenting agent to obtain third mixture; uniformly mixing third and first mixture, sealing, and fermenting; and adding mixture of amino acid powder and yeast powder and stirring.
NOVELTY - Preparing artesunate comprises adding ether solvent tetrahydrofuran ring artemisinin (or 1,3-dioxane or 1,4-dioxane) with potassium borohydride reducing agent (or lithium borohydride or zinc borohydride).    USE - Method for preparing artesunate (claimed).    ADVANTAGE - The method is simple, has low equipment requirement and convenient operation, and is environment-friendly and suitable for industrial production.
NOVELTY - Method for reducing emission of nitrous oxide during composting involves (a) composting raw material per ton by adding 20-40 kg biomass charcoal twice, where the first time, 10-20 kg biomass charcoal and the composting raw material are sufficiently mixed and placed in a composting tank and retaining the water content and carbon nitrogen ratio of the composting raw material, and the second time, 10-20 kg biomass charcoal is added and composting for 15-18 days, (b) chopping the composted material and intermittently turning the compost, and (c) fermenting the compost.    USE - The method is useful for reducing emission of nitrous oxide during composting (claimed) animal manure.    ADVANTAGE - The method is simple and cost-effective, and doesn't cause secondary pollution.    DETAILED DESCRIPTION - Method for reducing emission of nitrous oxide during composting involves (a) composting raw material per ton by adding 20-40 kg biomass charcoal twice, where the first time, 10-20 kg biomass charcoal and the composting raw material are sufficiently mixed and placed in a composting tank and retaining the water content to 60-70% and carbon nitrogen ratio of the composting raw material and composting for 20-25 days, and the second time, 10-20 kg biomass charcoal is added and composting for 15-18 days, (b) chopping the composted material and intermittently turning the compost either manually or mechanically, and (c) fermenting the compost at 60 degrees C or more for 30-45 days in at least 8 consecutive days.
NOVELTY - Purification of a natural gas comprises pressurizing the natural gas at 3-10 MPa, leading to an ionic liquid absorption chamber (4), controlling the temperature at 273-300K to obtain an imidazolium ionic liquid, and dissolving in absolute ethyl alcohol; leading the ionic liquid to a hydrate reactor (10), controlling the temperature at 273-275K, controlling pressure at 2.5-3.5 MPa, introducing to a drying chamber (12), and leading to the ionic liquid absorption chamber cyclic purification; and heating the chamber to 80 degrees C.    USE - Method for the purification of a natural gas (claimed).    ADVANTAGE - The method is simple, has less methane loss amount, and avoids secondary pollution.    DETAILED DESCRIPTION - Purification of a natural gas comprises:    (A) pressurizing a raw material natural gas at 3-10 MPa using a gas booster (1, 5), leasing to an ionic liquid absorption chamber (4), controlling the temperature at 273-300K to obtain an imidazolium ionic liquid, and dissolving in absolute ethyl alcohol to prepare a solution;    (B) leading the ionic liquid from the top of the ionic liquid absorption chamber to a hydrate reactor (10), controlling the temperature at 273-275K, controlling pressure at 2.5-3.5 MPa, if the natural gas purification index reaches 1J, introducing the natural gas to a drying chamber (12), leading to the ionic liquid absorption chamber cyclic purification until the natural gas sulfuric acid and carbon dioxide content reaches a commercial standard; and    (C) heating the ionic liquid absorption chamber to 80 degrees C, releasing absorbed gas, heating the hydrate reactor to 30 degrees C, and releasing hydration reaction gas.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of the method for the purification of a natural gas.    Gas booster (1, 5)    Temperature measuring instruments (3, 8)    Stirring device (9)    Hydrate reactor (10)    Drying chamber (12)
NOVELTY - Separation of ethane and ethylene comprises contacting mixed gas with suspension slurry in metal-organic framework material to obtain suspension slurry adsorbed with ethane and ethylene; carrying out gas stripping with C2 mixed gas to obtain replaced suspension slurry and mixed gas; and carrying out desorption to obtain ethane and ethylene.    USE - Method for separating ethane and ethylene (claimed).
NOVELTY - A microemulsified methanol diesel oil comprises 65-70 wt.% diesel; 10-15 wt.% water; 2-5 wt.% methanol; 8-10 wt.% emulsifier comprising 15-25 wt.% yeast, 15-25 wt.% flour enzyme, 5-15 wt.% sodium dodecylbenzenesulfonate, 5-15 wt.% fatty alcohol polyoxyethylene ether, 5-15 wt.% ethanol, 5-10 wt.% urea, 1-5 wt.% dimethylformamide, 1-5 wt.% potassium hydroxide, and 5-10 wt.% cyclohexylamine; and 5-10 wt.% cetane number improver.    USE - Microemulsified methanol diesel oil.    ADVANTAGE - The diesel oil is temperature resistant, has quietness, dispersity, antioxidation, anticorrosion, antifoaming, and pour point depressant, and does not layered and emulsified after long time storage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microemulsified methanol diesel oil by mixing oil solvent, ethylhexyl nitrate, nitromethane, alkyl nitrate, acetone, alkylphenol polyoxyethylene ether, nitro thinner, isooctanol, n-octanol, and oil spices in reaction tank, stirring to obtain cetane number improver, and storing for further use; mixing yeast, flour enzyme, sodium dodecylbenzenesulfonate, fatty alcohol polyoxyethylene ether, ethanol, urea, dimethylformamide, potassium hydroxide and cyclohexylamine in reaction tank, stirring to obtain emulsifier, and storing for further use; and mixing methanol and water in mixing tank, stirring for 40 minutes to obtain the denatured methanol, adding appropriate amount of denatured methanol, diesel, obtained cetane number improver and emulsifier, mixing, and allowing to stand for 4 hours.
NOVELTY - A multifunctional building comprises at least two residential buildings (1) and biogas digester (2) which is arranged between two adjacent residential buildings and is used for collecting and carrying out fermentation on human excrement and the wastes. A fruit tree section (3) is connected with marsh gas tank which is used for planting grape farm (4) and used for processing marsh gas in purifying center (5). The purifying center is used for preparing nutrient solution. An aerosol plant area is connected with nutrient liquid center.    USE - Multifunctional building for recycling energy.    ADVANTAGE - The building has rational design, saves social investment and product flow, recycles energy, and reduces environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a multifunctional building.    Residential buildings (1)    Biogas digester (2)    Fruit tree section (3)    Grape farm (4)    Purifying center (5)
NOVELTY - A solid catalyst biodiesel production line comprises feedstock oil pretreatment device through a pipe connection, esterification and transesterification reaction device, glycerin water separating device, and acid removal and distillation device. The whole production line is arranged in a container.    USE - Electric automatic control system for solid catalyst biodiesel production line (claimed).    ADVANTAGE - The control system has high degree of automation and can produce continuously.
NOVELTY - This utility model claims a sort of adsorption rough biological diesel oil refining device, wherein the refining device comprises a tower body (12), a tower body (12) is provided with an inlet valve A (1), the bottom is provided with an inlet valve B (7), an inlet valve A (1) and the inlet valve B (7) via the pipeline, the tower body (12) is provided with two parallel vertical baffle plate A (3), a baffle plate B (2), a baffle plate A (3) and the baffle B (2) of the tower body (12) is divided into the front adsorbent chamber (5), and the adsorbent chamber (10), the adsorbent chamber (10) corresponding to the tower body (12) is provided with a biological diesel oil outlet (9). The utility model not only effectively solves the problem that the existing biological diesel oil by water, complex process, and the waste gas generated in the water, resulting in the problem of environment pollution, but also effectively solves the problem that the biological diesel oil adsorption method, an adsorption tower to the fault, so as to influence the mass production of bio-diesel.
NOVELTY - A catalyst composition comprises 0.01-5 wt.% Group VIII noble metal element; 10-80 wt.% rare earth modified mordenite; 0.1-10 wt.% additive; and binder containing 0.5-5 wt.% sulfur, and 5-40 wt.% rare earth metal oxide.    USE - A catalyst composition used in the isomerization of 4-12C alkanes (claimed) for producing a blending component for high-octane gasoline.    ADVANTAGE - The catalyst composition has high catalytic activity, and has high isomeric olefin selectivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the binder, comprising mixing sulfate ions and aluminum hydroxide kaolin, drying and calcining to obtain sulfur-modified inorganic refractory oxide; and mixing the sulfur-modified inorganic refractory oxide, solvent, and deionized water.
NOVELTY - Jet fuel containing biomass fuel comprises alpha -pinene and jet fuel at 5-90:95-10 volume ratio, where the sum of the two components is 100 vol.%. The alpha -pinene has density of 0.85 g/cm3 at greater than or equal to 20 degrees C and freezing point at less than - 75 degrees C.    USE - Jet fuel containing biomass fuel.    ADVANTAGE - The jet fuel containing biomass fuel has better density and low temperature performance than that of the prior art, good performance, and simple preparation, uses reproducible raw material, and is easy to be produced on a large scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of jet fuel containing biomass fuel comprising adding the raw material i.e. alpha -pinene in a reactor filled with hydrogenation catalyst, conducting continuous or intermittent hydrogenation reaction, separating the hydrogenation catalyst, and mixing the synthetic biomass fuel and aviation kerosene or kerosene rocket fuel at 5-90:95-10 volume ratio to obtain the product. The hydrogenation catalyst is 5-20 wt.% nickel/silicon dioxide, 2-5 wt.% palladium/alumina, 1-5 wt.% palladium on carbon, or Raney nickel. The continuous hydrogenation reaction is conducted at 150-300 degrees C, 2-5 MPa, hydrogen and alpha -pinene volume ratio of 200-1000:1, and hydrogen volume space velocity of 1-5/hour. The intermittent hydrogenation reaction is conducted at 80-200 degrees C, 1-5 MPa, and hydrogenation catalyst amount of 1-15 wt.% based on the amount of alpha -pinene for 2-10 hours.
NOVELTY - Biodiesel oil adjusting mixture comprises colorless product, number 0 diesel, and ashless dispersant, which are uniformly mixed at 65-75 mass%:24.8-34.7 mass%:0.1-0.4 mass%. The colorless product is produced by treating 10C distillate by hydrogenation separation, where 10C distillate is a by-product of an ethylene unit. The ashless dispersant is a mixture of succinimide and polyisobutylene succinimide at 1:1 mass ratio.    USE - Adjusting mixture used for biodiesel oil (claimed).    ADVANTAGE - By adding the biodiesel oil adjusting mixture in biodiesel oil, the freezing point of biodiesel is reduced by 5-10 degrees C and exhaust gas carbon content is reduced by 20-25%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of biodiesel oil adjusting mixture comprising adding 20-35% biodiesel oil adjusting mixture in biodiesel.
NOVELTY - Municipal domestic sewage sludge clean fuel processing system comprises concentrating tank, concentrated sludge performance testing mechanism, mixing reactor, mechanical extrusion drying mechanism, combustion boiler, gas treatment device, heat supply system, sludge-pulverized coal ash disposal treatment system, condensing device, denitrifying device, desulfurizing device, ammonia-removing device and aqueous ammonia storage tank.    USE - Municipal domestic sewage sludge clean fuel processing system.    ADVANTAGE - The system and the method are environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for municipal domestic sewage sludge clean fuel processing comprising:    (A) concentrating municipal domestic sewage sludge in concentrating tank, conveying into concentrated sludge performance testing mechanism, conveying into mechanical extrusion drying device, adding combustion accelerant and additive A, kneading with coal to desired shape to obtain semi-finished product and drying;    (B) mixing with modifier in mixing reactor, adding additive B and coal powder to obtain slurry and entering into combustion boiler;    (C) conveying gas generated into gas treatment device and conveying sludge and pulverized coal ash into sludge-pulverized coal ash disposal treatment system;    (D) testing if aluminum content is more than 6.40% or iron content is more than 1.90% and directly preparing into low-molecularity flocculating agent for building material or roadbed material; and    (E) denitrifying residual gas in denitrifying device, desulfurizing in desulfurizing device, removing ammonia in ammonia-removing device and conveying removed ammonia into aqueous ammonia storage tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of municipal domestic sewage sludge clean fuel processing system (Drawing includes non-English language text).
NOVELTY - Continuous separation of biodiesel oil comprises conveying biodiesel oil and glycerol mixed solution through liquid distributor (1) into shock-proof cavity (3), entering into first-stage sedimentation chamber (4), adjusting first water bath temperature control area (5) to 40-55 degrees C, entering into second-stage sedimentation chamber (6), adjusting second water bath temperature control area to 10-40 degrees C, adjusting biodiesel oil flow in biodiesel oil outlet (9) and adjusting glycerol phase liquid level height.    USE - Continuous separation of biodiesel oil (claimed).    ADVANTAGE - The method has convenient operation and high separation degree.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device used for continuous separation of biodiesel oil comprising liquid distributor (1), condensing device (2), shock-proof cavity (3), first-stage sedimentation chamber (4), first water bath temperature control area (5), second-stage sedimentation chamber (6), second water bath temperature control area (7), receiver connector (8), biodiesel oil outlet (9) and glycerol outlet (10).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device used for continuous separation of biodiesel oil.    Liquid distributor (1)    Condensing device (2)    Shock-proof cavity (3)    First-stage sedimentation chamber (4)    First water bath temperature control area (5)    Second-stage sedimentation chamber (6)    Second water bath temperature control area (7)    Receiver connector (8)    Biodiesel oil outlet (9)    Glycerol outlet (10)
NOVELTY - One-step bifunctional ionic liquid catalytic preparation of biodiesel oil from waste oil comprises reacting waste oil and alkyl alcohol at 50-160 degrees C for 1-6 hours in the presence of alkaline ionic liquid as catalyst.    USE - One-step bifunctional ionic liquid catalytic preparation of biodiesel oil from waste oil (claimed).    ADVANTAGE - The simple method has low cost, mild reaction condition, short reaction time and no pollution. It uses catalyst having high activity and good thermal stability at lesser dosage.
NOVELTY - A bio-preparation method of methyl 3-amino-4-(2,4,5-trifluorophenyl)butyrate involves: reacting methyl 3-oxo-4-(2,4,5-trifluorophenyl)butyrate as substrate with cofactor, amino donor and auxiliary solvent in a biological catalyst comprising a recombinant aminotransferase.    USE - In preparing methyl 3-amino-4-(2,4,5-trifluorophenyl)butyrate (claimed), for treating metabolic disorders including cancer.    ADVANTAGE - The method has low energy consumption, simple and convenient operation, provides methyl 3-amino-4-(2,4,5-trifluorophenyl)butyrate with high optical activity with little by-product.    DETAILED DESCRIPTION - A bio-preparation method of methyl 3-amino-4-(2,4,5-trifluorophenyl)butyrate involves: reacting methyl 3-oxo-4-(2,4,5-trifluorophenyl)butyrate as substrate with cofactor, amino donor and auxiliary solvent in a biological catalyst to obtain 3-amino-4-(2,4,5-trifluorophenyl)butyrate; where the biological catalyst is a recombinant aminotransferase. The recombinant aminotransferase is prepared by inoculating single bacterial colony in kanamycin resistance LB liquid culture medium and activating for 8-12 hours; activating the obtained culture at 35-40 degrees C and expanding culture to reach 0D600 value of 0.6-0.8; adding inducer and continuously culturing at 8-12 degrees C for 25-35 hours, centrifuging, collecting precipitate, adding phosphate buffer solution to obtain the suspension, crushing the suspension in ultrasonic ice bath for 8-12 minutes, then centrifuging the supernatant and freezing the supernatant fluid at -1 degrees C to 25 degrees C, and then drying for 24-48 hours, to obtain the recombinant aminotransferase, where the reaction is carried out at pH of 6-9 which is adjusted using a water phase buffer solution.
NOVELTY - A biological diesel oil is prepared by, in the presence of lipase aqueous solution, crushing raw material grease with monohydric alcohol reaction, a mole ratio of monohydric alcohol and hydrolysate fatty acid being 1-3:1; adding 100-500 unit lipase aqueous solution (200-1000 unit/ml- degrees C), and reacting at 20-60 degrees C for 4-20 hours; and separating upper layer oil phase and aqueous phase lipase and glycerol.    USE - Method for preparing biodiesel oil (claimed).    ADVANTAGE - The method provides for low acid value and high conversion rate of biological diesel oil, has mild reaction condition and low energy consumption, and is suitable for large-scale industrial production.
NOVELTY - Production of palm biodiesel oil comprises fractionating methyl ester and/or ethyl ester at 5-30 Pa, subjecting methyl ester and/or ethyl ester to dry crystallization, or subjecting methyl ester and/or ethyl ester to solvent crystallization.    USE - Production of palm biodiesel oil i.e. saturated palm oil methyl ester (claimed).    ADVANTAGE - The pour point of palm biodiesel oil is greater than or equal to 15 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of saturated palm oil methyl ester comprising subjecting methyl ester and/or ethyl ester to dry crystallization or solvent crystallization, where saturated palm oil methyl ester contains greater than or equal to 85-90% methyl palmitate.
NOVELTY - Production of methanol synthesis gas involves dividing water gas into three portions of 10-50 volume% portion (A), 10-40 volume% portion (B) and 35-60 volume% portion (C), converting the portion (A) to gas (a) containing carbon dioxide and hydrogen in a carbon monoxide conversion reactor, allowing the portion (C) into a gas separation device, obtaining gas (c) containing carbon monoxide and gas (d) containing hydrogen, and allowing the portion (B), gas (a) and gas (d) into acid-gas cleaning device for removing sulfide and portion of carbon dioxide.    USE - Production of methanol synthesis gas (claimed).    ADVANTAGE - The method efficiently provides methanol synthesis gas.    DETAILED DESCRIPTION - Production of methanol synthesis gas involves using water gas as a raw material, dividing the raw material into three portions of 10-50 volume% portion (A), 10-40 volume% portion (B) and 35-60 volume% portion (C), allowing the portion (A) to carbon monoxide conversion reactor for converting the water gas to gas (a) containing carbon dioxide and hydrogen, allowing the portion (C) into a gas separation device, obtaining gas (c) containing carbon monoxide and gas (d) containing hydrogen after separation, discharging the gas (c), allowing the portion (B), gas (a) and gas (d) into acid-gas cleaning device for removing sulfide and portion of carbon dioxide, and obtaining methanol synthesis gas.
NOVELTY - Solvent foaming of natural gas amine desulfurization comprises entering raw material gas into hydrogen sulfide absorption tower in contact with desulfurization solution, processing gas-liquid micro-rotational flow separation to remove raw material gas in solid particle impurity and more than 4C heavy hydrocarbon to obtain purified natural gas, passing through hydrogen sulfide absorption tower, carrying-out gas-liquid micro-cyclone separation and purifying natural gas in a solvent.    USE - Method of solvent foaming of natural gas amine desulfurization (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the solvent foaming of natural gas amine desulfurization.
NOVELTY - Preparation of propylene comprises removing isobutane and n-butane in raw material by extracting to obtain olefin stream I, alkene stream I with isomerization catalyst to contact and react to obtain slurry with stream II, mixing stream II and boundary zone of fresh ethylene stream III and obtaining adsorbent; and contacting and reacting stream III a disproportionation catalyst to obtain product propylene, entering stream IV into ethylene tower, entering stream V to propylene removing tower, and taking product from tower top.    USE - Method of preparation of propylene (claimed).    ADVANTAGE - The method is suitable for industrial production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the preparation of propylene.
NOVELTY - Lowering freezing point of biodiesel crude product comprises taking biodiesel crude product with acid value of 3-20 mg potassium hydroxide (KOH)/g, carrying out continuous contact reaction of biological diesel oil crude product with monohydric alcohol, in the presence of catalyst at reaction conditions of 70-220 degrees C, 2-3 MPa and amount of catalytic agent is 0.001-0.4 wt.% of biodiesel crude product.    USE - Method for lowering freezing point of biodiesel crude product (claimed).    ADVANTAGE - The acid value of biological diesel oil is less than 0.8 mg KOH/g.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological diesel oil which comprises taking crude product biological diesel oil with acid value of 3-20 mg KOH/g, reducing, decompressing and distilling.
NOVELTY - Reducing acid value of biodiesel crude product with acid value of 3-20 mg potassium hydroxide (KOH)/g comprises carrying out contact reaction of biological diesel oil coarse product with monohydric alcohol in the presence of catalyst at conditions of 70-200 degrees C and 0.1-1 MPa, and amount of catalyst is 0.001-0.3 wt.% of biodiesel crude product.    USE - Method for reducing acid value of biodiesel crude product (claimed).    ADVANTAGE - The acid value of biological diesel oil is less than 0.8 mg KOH/g.
NOVELTY - Low oil consumption methanol gasoline comprises 25-35 wt.% denatured methanol, 40-60 wt.% gas oil and 10-30 wt.% heavy oil. The relative density of finished product is 0.75-0.76. The denatured methanol is prepared by mixing 100 pts. wt. methanol and 5 pts. wt. additive. The additive is obtained by mixing 20 pts. wt. methyl tert-butyl ether, 30 pts. wt. toluene, 20 pts. wt. acetone, 10 pts. wt. emulsifier op-80 and 20 pts. wt. n-butanol. The heavy oil density is greater than gasoline density and light oil density is lower than gasoline.    USE - Low oil consumption methanol gasoline.    ADVANTAGE - The gasoline does not need antiknock component, and octane value is 96-105.
NOVELTY - The apparatus has drug jet nozzle unit (80) in which a hole is formed, and drain tank is installed at a bottom side of stirred tank. The food waste (W) and wood chip (C) are stirred in the stirred tank inside a heater portion. A showering nozzle unit (70) is installed at upper end of stirred tank to spray water to stirred tank. Multiple sensors are provided for measuring temperature of stirred tank. The food waste is provided in the bottom surface of stirred tank for processing by the microorganism.    USE - Disposal apparatus for waste food.    ADVANTAGE - The stirred tank is heated at in the meantime to optimize the temperature environment of the microorganism and the water is supplied to the stirred tank in to optimize the humidity environment of the microorganism, so that the microorganism can be made to decompose and process the food waste efficiently. The food waste of many amounts can be processed within the fast time. The food waste spraying the drug and the bad smell component can be completely removed.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the disposal apparatus for waste food.    Door (12)    Showering nozzle unit (70)    Drug jet nozzle unit (80)    Wood chip (C)    Food waste (W)
NOVELTY - A pyroligneous liquor is prepared by heating oak trees in charcoal kiln at 350-400 degrees C, generating smoke, liquefying smoke at 85-120 degrees C and maturing the liquefied liquid for 3-6 months. Then, herbicidal composition containing 2 g flazasulfron, 50 ml pendimethalin, 50 ml bentazone, 10 ml spreader sticker, and 400 ml pyroligneous liquor, is prepared and sprinkled on lawn, to suppress weeds.    USE - Method for suppressing weeds (claimed).    ADVANTAGE - The method environmentally-friendly enables suppression of weeds.
NOVELTY - A plant material is fed into microwave vacuum tank which is evacuated with vacuum degree of 0.001 Mpa, then treated using microwaves with microwave frequency of 300-950 MHz for 1-3 minutes. The pre-treated plant material is dried, pre-carbonized, carbonized, calcined, cooled, warmed to control the combustion rate to 5-15 degrees C/minute, heated at 700-750 degrees C or 900-1000 degrees C for 40-80 minutes with rate of 5-15 degrees C/minute and then further heated to 1000-1500 degrees C or 1600-1800 degrees C for 2-8 hours. Then, plastic is added to mixture and processed to obtain plant-derived plastic material.    USE - Preparation of plant-derived plastic material (claimed).    ADVANTAGE - The method efficiently and economically provides plant-derived plastic material having high rigidity, toughness, antistatic property and flame resistance.    DETAILED DESCRIPTION - A plant material is fed into microwave vacuum tank which is evacuated to 0.02 MPa gauge with vacuum degree of 0.001 Mpa, then treated using microwaves with microwave frequency of 300-950 MHz for 1-3 minutes. The pre-treated plant material is dried, pre-carbonized, carbonized, calcined, cooled, warmed to control the combustion rate to 5-15 degrees C/ minute, heated at 700-750 degrees C or 900-1000 degrees C for 40-80 minutes with rate of 5-15 degrees C/minute and then further heated to 1000-1500 degrees C or 1600-1800 degrees C for 2-8 hours. Then, plastic comprising 100 pts. wt. polypropylene having molecular weight of 400-700 million, 30-35 pts. wt. polypropylene having molecular weight of 100-140 million, 3-12 pts. wt. flame retardant, 5-10 pts. wt. plasticizer, 2-5 pts. wt. coupling agent, 0.5-1 pts. wt. antioxidant and 15-20 pts. wt. plant material is added to mixture and processed to obtain plant-derived plastic material.
NOVELTY - This utility model claims a kind of livestock excrement biological decomposing processor, comprising a stirring tank, a stirring shaft and a plurality of blades, the stirring shaft is installed in the stirring groove whose two ends are respectively fixed connected with the stirring groove, one end of the plurality of vanes are uniformly fixed on the stirring shaft and is vertical to the stirring shaft, the multiple blades are uniformly distributed on the circumference of the stirring shaft, and a plurality of the blade length is grown is short, then a step size change is. This utility model is a kind of biological decomposition livestock manure, livestock manure with bacterium of composite function adequately, and the strain fully contact oxygen, this method is not easy to generate dead angle to the livestock manure with the microorganism fully contact, at the same time bacterium of composite function fully contact oxygen, propagation of beneficial bacterium of composite function, so as to accelerate the degradation speed dejection of poultry.
NOVELTY - This utility model claims a household garbage processing device, comprising a stirring tank, which is filled with solid waste and particulate ball, the stirring tank is provided with a stirrer, the stirrer comprises a horizontal shaft and set on the upper of the connecting rod, the connecting rod is fixed with a rotation of, the stirring tank is further provided with a heating device and an air adjusting device are respectively provided with a feeding port and a discharging port on the upper part and the bottom of the stirring tank, the particle is porous spherical structure. This utility model of the particle ball of the whole outer surface of a fine concave-convex friction resistance is large, the household garbage can be adequately grinding in a short time, and it will not mutual adhesion, does not need to periodically add and saves the cost.
NOVELTY - This utility model claims a biomass carbon gas cogeneration device, comprising a carbonizing device, a condensing device, a water washing device, a dehydrating device, a drying device, a liquid collecting device, a detecting device and a storage device, wherein the carbonizing device from the combustible gas enters the condensing device, a water washing device, a dehydrating device, a drying device, and the generated filtrate enter into liquid collecting device, the gas oxygen content detection device for detecting less than or equal to 4%, then the qualified gas to a gas storage device. The beneficial effect of the utility model is a combustion gas purifying effect is good, high heat value of combustible gas, can make full use of the biomass energy, equipment sleeve, provided complete is reasonable, the operation is simple and convenient.
NOVELTY - A static aerobic ferment organic compost device, belonging to the manure fermentation device, wherein the device is a cylindrical end of the through hole, the bottom is provided with the cylinder circumference uniformly distributed ventilation opening is provided with an inner annular slot at the lower part of the cylinder, the annular groove is placed above the air of the arched net-shaped surface. The device is provided with organic stack adequately , whole ferment uniform. With no turning in the fermentation process, labour investment, low labour intensity, organic matter fermentation temperature, long lasting time, effective to kill virus and harmful microorganism, organic matter fermented need short time and removing smell, no pollution, beautiful, clean and so on, which is suitable for peasant household farmyard organic fertilizer fermentation.
NOVELTY - This utility model claims a kind of biomass cooking heating double-purpose furnace. A furnace body is set in the hearth, the inner side wall of the furnace body is provided with a water inlet of the water jacket, the furnace body is provided with feed inlet of hearth, the lower part is provided with a movable furnace grate, lower grate is provided with an ash hopper, a secondary oxygenation cavity at lower part of the hearth is divided into first combustion chamber and the upper part of the secondary combustion chamber, the secondary combustion by the secondary oxygenation cavity is provided with a combustion-supporting hole, the furnace body is further provided with a smoke box with a water outlet is connected with the water sleeve of the flue passes through the water tank, the flue is connected with hearth and smoke at the same time is connected with the water tank by the hot water pipe in the flue, the furnace body is further provided with a storage bin, the storage bin is inclined downwards is connected with the hearth, the feeding port is set on the top of the storage bin. This utility model does not need combustion-supporting device, and the furnace end are separately set, capable of continuously feeding continue without interruption, and it will not cause smoke from entering the room, pollute the indoor environment.
NOVELTY - Producing biogas in anaerobic digestion by pre-treating sludge through steam explosion comprises: (i) passing dehydrated sludge into a gas explosion machine, introducing saturated water vapor inside the machine at 150-200 degrees C for 2-10 minutes at a pressure of 0.8-2 MPa, opening a gas valve of the machine and collecting the discharged materials; and (ii) adding 3-50 wt.% inoculum into the pre-treated material, stirring uniformly, sealing and fermenting.    USE - The method is useful for producing biogas in anaerobic digestion by pre-treating sludge through steam explosion (claimed).    ADVANTAGE - The method improves the biodegradability of the sludge which is good for degradation of microorganisms; and improves the utilization rate and gas production rate of the sludge.
NOVELTY - The system has a main shaft whose upper end is provided with ash hoe water cooling fire grate. An ash hoe inner part is connected with the main shaft via a circulating pipe. The circulating pipe is connected with an upper water pipe and a lower water pipe. An upper water pipe inlet end is connected with a circulating water inlet pipe via a main shaft wall. The lower water pipe is connected with a circulating water outlet pipe by the main shaft. The water cooling fire grate is connected with a hollow coil pipe. The circulating water inlet pipe is connected with a water inlet seal head.    USE - Down-sucking type biomass fixed bed continuous pyrolysis furnace water cooling fire grate system.    ADVANTAGE - The system is simple in structure, and has high strength and prolonged service life of the water cooling fire grate, and realizes ash and dust cleaning phenomenon when rotating the main shaft so as to improve working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a water cooling fire grate.
NOVELTY - The method involves generating biomass fuel gas in a gasification furnace. A gas channel is arranged on an upper part of the gasification furnace. A spacing unit is cooled in the gas channel. A cooling medium passage is arranged in the gasification furnace. A shell inlet and outlet of the cooling medium passages are located in the gasification furnace. A cooling pipe is provided with a downlink channel and an uplink channel. A thick pipe is sleeved on a thin tube that is formed as the downlink channel. The thick pipe is formed as the uplink channel.    USE - Method for removing tar biomass fixed bed gasification furnace.    ADVANTAGE - The method enables avoiding influence production efficiency of the gas and pollutes external environment and circulating water, improving the energy utilization rate, reducing cooling loss and saving the investment cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for removing tar biomass fixed bed gasification furnace.
NOVELTY - Double-carbonization type high-temperature carbon baking method involves carbonizing a biomass raw material primarily, retaining substances capable of being decomposed to generate wood tar and bonding carbon particles, then compressing and forming a carbon product obtained through primary carbonization, carbonizing the obtained formed carbon product secondarily, and then obtaining high-temperature carbon The secondarily carbonization temperature is more than the primary carbonization temperature.    USE - Double-carbonization type high-temperature carbon baking method (claimed).    ADVANTAGE - The method is carried out efficiently and economically.
NOVELTY - Preparation of pesticide involves using chitin biomass waste as raw material, performing pyrolysis on the raw material, and heating and decomposing the obtained pyrolysis liquid under vacuum or anoxic condition.    USE - The method is useful for preparing pesticide (claimed) used for providing antibacterial effect and promoting growth of plants.    ADVANTAGE - The method is simple and cost-effective, utilizes waste chitin biomasses and prepares pollution-free pesticide which has broad antibacterial spectrum and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of above-cited pesticide which involves (a) placing the chitin biomass waste into a vacuum pyrolysis reactor, vacuumizing, heating to 220-600 degrees C, vacuumizing continuously, where the pyrolysis product is gaseous at high temperature, pumping the gaseous pyrolysis product continuously using vacuum pump, taking out from the reactor and placing in a collector, condensing using thermal hydrolysis to obtain pyrolysis liquid and (b) adding 0-3.5 times water to the obtained pyrolysis liquid, mixing uniformly, allowing the mixture to stand for 3-24 hours, filtering and removing residue, and adding 0.5-15% non-polluted surfactant to the filtrate.
NOVELTY - The device has a water electrolytic cell, hydrogen and oxygen separators, a cooler, a hydrogen and oxygen gas cooler and an alkaline liquor circulating pump that are connected with each other. A tensioning screw rod of an electrolytic chamber is connected with a pressing end of a pressing plate. A PLC program controller and a control instrument are connected with each other. A shell-and-tube heat exchanger is connected with a liquid moving pipe. A system meter is connected with the shell-and-tube heat exchanger tube.    USE - Water electrolysis hydrogen production device.
NOVELTY - Preparing liquid micro-organism organic fertilizer by using animal blood enzymolysis and de-foaming agent involves mixing animal blood as fermentation substrate, proteolytic enzyme and bacteria liquid; prior to implantation microbial strain, heating and sterilizing the raw material and auxiliary material, and adding antifoaming agent, effectively eliminating removing scum, adding the organic phosphorus content in the same kettle, performing first enzymolysis, aerobic fermentation, and anaerobic fermentation to form liquid micro-organism organic fertilizer.    USE - For preparing liquid micro-organism organic fertilizer (claimed) for promoting development of root system; and improving resist disease.    ADVANTAGE - The method prevents the material overflowing loss, and avoids secondary environment pollution.    DETAILED DESCRIPTION - Preparing liquid micro-organism organic fertilizer by using animal blood enzymolysis and de-foaming agent involves mixing 1000 ml animal blood in the sterilization tank, 100-200 kg brown sugar, 100-200 kg of white sugar, and slaughterhouse clean blood draining groove organic waste water to prepare 800-1500 kg sugar water mixed solution; adding the sugar water mixed solution into the sterilizing tank, mixing and stirring the animal blood, raising the temperature to 100 degrees C, sterilizing for 0.5-1 hours, continuously adding defoaming agent; reducing the temperature, transferring thr mixture to the fermentation tank; adding 2.5-5.4 kg water at 50 plus minus 2 degrees C; performing enzymolysis for 4-6 hours, reducing the temperature to 38 plus minus 2 degrees C, stirring and adding 10-15 kg adding strain liquid, performing aerobic fermenting for 10-12 hours, cooling, closing the filter, performing anaerobic fermentation for 13-15 hours; performing sample testing viable count reaches 2 billion/ml, measuring pH value of 5-6 to form liquid micro-organism organic fertilizer.
NOVELTY - Dehydrated sludge and aqueous decomposing agents are mixed, deodorant spray process is performed to remove odor, crushed and mixed with combustion-supporting additives, biomass auxiliary fuel and pulverized coal powder, to obtain sludge coal. The aqueous decomposing agent comprises red mud, sodium salt, bentonite and organic flocculants in the weight ratio of 1:1-2:1-2:1-2, respectively. The combustion-supporting additives are strong organic-oxidizing agent, magnesium, rare-earth and sodium humate in the weight ratio of 1:1-2:1-2:1-2, respectively.    USE - Manufacture of sludge coal (claimed).    ADVANTAGE - The method provides sludge coal by simple and economical process.
NOVELTY - This utility model claims a kind of disease livestock and poultry dead innocent processing system, comprising a crushing stirrer, fermentation, the fermentation processing machine is provided with a feeding port and a discharging port of the shell, heating device, water, a heating unit, a shell body is equipped with stirrer, heating device is connected to the shell by the pipe, sprinkler is connected to the shell by the pipeline, wherein the heating unit comprises a fan and a heater, a heating unit is hot air into the shell by the pipeline, wherein the crushing stirrer is provided with a feeding port and a discharging port, the stirring machine is connected with the material feeding port of the fermentation processing machine shell through the discharging transmission device, the system may also include a discharge port of the extruder, extruder is connected the feeding port of the fermentation processing machine shell through the discharging transmission device, the fermentation processing machine further comprises an automatic temperature control unit for controlling temperature in the shell body. The utility model can the disease livestock and poultry dead effective to convert to stable quality of organic fertilizer, strong processing ability, and the cost is low.
NOVELTY - A kind of used for agriculture and forestry waste aerobic composting of blast air device, wherein it comprises a fan (1), a connecting opening (2), a PVC pipe (3), the vent hole (4), the choke plug (5), a blower (1) to the lower end through the connecting opening (2) is connected with the PVC pipe (3), a PVC pipe (3) is uniformly provided with multiple vent holes (4), a PVC pipe (3) is provided with a choke plug (5). It can pass through the air vent to the stack for oxygen, which is good for forming the material air hole, to make the material keep fluffy, the equipment investment is low, temperature and ventilation condition to obtain better control of the composting time is relatively short, it can effectively kill pathogenic bacteria and odour control, at the same time, the influence of the cold climate.
NOVELTY - The reaction kettle has an outer casing of steel pressure container (1). A feeding port is set on the upper portion of the outer casing. The lower portion of the outer casing is provided with an inverted conical end enclosure (2). A jacket is provided on the outer casing.    USE - Reaction kettle for performing biomass gasification.    ADVANTAGE - The biomass gasification reaction and reactions of the materials are performed at central region of the reaction kettle, thus complete reaction of the materials is realized, so that required production object is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reaction kettle.    Steel pressure container (1)    Inverted conical end enclosure (2)
NOVELTY - The static aerosol removal apparatus (200) has pyrolysis product inlet (402) that is used for inputting a pyrolysis product containing pyrolysis gas and aerosol generated by biomass pyrolysis. The wet-type static absorption units are provided between anodes and cathodes, for absorbing the aerosol of different size. A pyrolysis gas outlet (420) is used for outputting the pyrolysis gas. A spray cleaning device is used for cleaning the static absorption units.    USE - Static aerosol removal apparatus for biomass pyrolysis generation fuel system (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass pyrolysis generation fuel system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the static aerosol removal apparatus. (Drawing includes non-English language text)    Static aerosol removal apparatus (200)    Cylinder (400)    Pyrolysis product inlet (402)    Pyrolysis gas outlet (420)    Pump (422)
NOVELTY - Synthesis of beta -artemether involves reacting dichloromethane alkaline aqueous solution in presence of sodium borohydride as reducing agent and aluminum tert-butoxide as catalyst and obtaining dihydroartemisinin, removing aqueous phase, and adding methanol, sodium hydrogen sulfate, aluminum perchlorate and nickel perchlorate as catalyst for methyl etherification reaction, and reacting for 2 hours at room temperature.    USE - Synthesis of beta-artemether (claimed).    ADVANTAGE - The method efficiently and economically provides beta -artemether with yield of 93.5%, in short period of time using simple process.
NOVELTY - This utility model claims a high efficiency condensing heat energy of waste water using system, especially a condensed water circulation efficient use in ammonium phosphate workshop of the system. The system is composed of a condensed water heater, an auxiliary gas-liquid separating tank, a liquid ammonia evaporation station and drying tower hot air exchanger is composed of four parts, condensed water heater in series connected with auxiliary gas-liquid separating tank, an auxiliary gas-liquid separating bottom tank in series is connected with the liquid ammonia evaporation station, a tank top are connected in series of the drying tower hot air exchanger, the working time, the condensed water after being heated by condensed water heater through auxiliary gas-liquid separating tank, an auxiliary gas-liquid separating tank for steam and hot water separated from the steam collecting and flow-collecting device for spray drying tower hot air exchanger in the tank, the heat water in the bottom of the tank and flows into the liquid ammonia evaporation station. This utility model patent greatly improves the heat energy utilization efficiency of the condensed water, so as to save a large amount of energy and protects the environment, which is good for optimizing management system.
NOVELTY - Disproportionating hydrocarbons, comprises reacting pentanes in contact with ultrastable zeolite Y having a silica to alumina ratio of less than 80 to disproportionate the pentanes into butanes and hexanes, where the ultrastable zeolite Y has a sodium oxide content of less than 1 wt.%.    USE - The method is useful for disproportionating hydrocarbons into butanes and hexanes (claimed).    ADVANTAGE - The method: converts at least 20% of the pentanes; regenerates the ultrastable zeolite Y (all claimed); utilizes the zeolite Y, which exhibits improved selectivity, lifetime and thermal stability; avoids the occurring of undesired cracking reactions; and provides the butanes and hexanes with high purity.
NOVELTY - A ditch used for draining domestic sewage is arranged in ground, plants growing in water are planted in the ditch, microorganism purification groups which grow naturally are cultured, and a low-lying land used for reed planting is formed on a drainage outlet of the ditch. The plants growing in water absorb eutrophic composition in domestic sewage. The microorganism purification groups decompose organic matter and purify a portion of substances in water, reed at the drainage outlet of the ditch block, impurities, and deposited suspended matter.    USE - Purification of domestic sewage discharge (claimed).    ADVANTAGE - The method naturally forms a facility capable of purifying sewage for a long period of time, and saves purification cost.
NOVELTY - Biological enzyme treating agent of industrial wastewater comprises 10-18 pts. wt. oxidoreductase, 10-15 pts. wt. cellulase, 5-8 pts. wt. protease, 5-8 pts. wt. laccase, 6-8 pts. wt. methane producing Corynebacterium ammoniagenes, 6-8 pts. wt. nitrifying bacteria, 0.5-1.5 pts. wt. bamboo juice, and 100 pts. wt. water.    USE - As biological enzyme treating agent of industrial wastewater.    ADVANTAGE - The agent is environmentally-friendly, saves energy, reduces operating cost for processing wastewater, enables to purify wastewater with stable quality, purify polluted substances and degrade liquid pollutants rapidly, reduce the size of solid substances, and remove foul smell from the wastewater.
NOVELTY - Processing sewage using biological agent, comprises introducing raw sewage into a grid neutralization tank, performing gas explosion treatment by adding Bacillus subtilis, introducing the treated sewage into an iron-carbon treatment tank, adjusting pH value of the sewage to 7.5, introducing the sewage and adding a biological agent into a biological treatment tank, treating for 3 days and discharging the treated sewage, where the grid neutralization tank, the iron-carbon treatment tank and the biological treatment tank are planted to maintain water discharge pressure difference.    USE - The method is useful for processing sewage using biological agent (claimed).    ADVANTAGE - The method has low infrastructure investment, good sewage treatment effect, no secondary pollutions, and lower energy consumption when compared with the regular sewage treatment process, and hence develops low carbon economy, high efficiency, environmental protection and recycling economy; and reduces treatment cost due to the adoption of the biological agent.
NOVELTY - The method involves performing a tank fermentation process, a tank air separation process and a pool natural biological bacteria film grid process for realizing the recycling of the domestic sewage.    USE - Domestic sewage treatment method.    ADVANTAGE - The operation time for domestic sewage treatment can be shortened effectively while significantly reducing the production and operation costs. The sewage treatment stability and sewage water quality can be improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the domestic sewage treatment device.    Rushing channel (1)    Vertical biological tank (2)    Flow channel (3)    Greenbelt (4)    Biological stuffing frame (5)
NOVELTY - An ethyl salicylate glycoside compound (I), and its isomer and fully acetylated compound, is new.    USE - The compound is useful in pharmaceutical composition for preparing antipyretic, antiinflammatory, analgesic and antithrombotic drugs, and drugs for preventing platelet aggregation. The pharmaceutical composition is in the form of tablet, capsule, pill, injection, extended-release preparation, controlled release preparation and various particulate delivery systems (all claimed).    ADVANTAGE - The compounds have prolonged therapeutic effect and reduced adverse reaction as compared with salicylic acid medicaments, and suppresses stimulation to the gastrointestinal tract. The method is simple to perform, cost-effective and environmentally-friendly as it causes less environmental pollution.    DETAILED DESCRIPTION - An ethyl salicylate glycoside compound of formula (I), and its isomer and fully acetylated compound, is new.    R=monosaccharide and oligosaccharide.    An INDEPENDENT CLAIM is included for method for preparing the compound.
NOVELTY - A kind of thin film fixed bed method for preparing biological diesel oil device, belonging to the field of chemical device manufacturing technology field of plant oil tank, methanol tank, a stirring tank, a reaction tower, a separating tower, a cooling tower, a storage tank, a centrifugal pump, a pumping tank, storage tank, a storage tank and a condensing tower system, the work time, animal and vegetable oil and methanol into stirring tank for mixing uniformly, the reaction tower is heated and enters the reaction bed to process esterification reaction under the action of catalyst, then entering into the separation tower, and deposited on the floating in glycerol, over flow into a cooling tower, a and a cooling storage tank, then purified by centrifugal pump and pumping tank to obtain the pure methyl ester biologic diesel oil product into a storage tank, wherein a reaction container the methanol gas is cooled into liquid, returning the methanol tank by the cooling tower. This utility model conversion rate is high, there is no waste water, waste slag discharge, which meets the requirement of environmental protection.
NOVELTY - Preparation of water hyacinth biogas involves using mesophilic anaerobic fermentation technology as a basic process, chopped flexible material, biological acidification, nitrogen nutrient supplement and other technical measures.    USE - For preparation of water hyacinth biogas for water hyacinth energy plant (claimed).    ADVANTAGE - The method produces water hyacinth biogas with high efficiency; belonging to the field of environment protection and biomass energy field; improves the conversion rate of organic carbon into methane, the organic load reactor is improved by 2-5 times, the residence time is shortened to 1 days, yield volume to 1.5 m3/m3/day, fresh ton gas rate is more than 25 m3, so as to accelerate the water hyacinth biogas production speed in a company for operation as the plant to use.
NOVELTY - The system (10) has an electrolyzer core (12) that generates hydrogen and oxygen gases. The electrolyzer core includes a water electrolyzer (14). An electrolyte container (22) that is provided with electrolytes (24) is connected to electrolyzer core with supply tube (26) and return tube (28). The electrolytes in electrolyzer core are released into electrolyte container through supply tube, when gases are released. The electrolytes are allowed to enter electrolyte core through return tube such that electrolyte is forced to circulate by releasing force of gases.    USE - Pumpless, fanless electrolyte-circulation system for hydrogen generator used in vehicle (claimed).    ADVANTAGE - The system can prevent the electrolyte from overheating and can cool the electrolyte without any pump or fan since the electrolytes are forced to circulate by releasing force of gases. The system is simple and cost effective since the use of pump and fan is eliminated. The temperature sensor can ensure that the system operates within suitable pre-set range of temperature since the controlling module powers the system off, when the temperature sensor reads suitable pre-set minimum value or pre-set maximum value of the temperature. The system can operate properly according to suitable pre-set range of power since an amperage sensor is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a pumpless, fanless electrolyte-circulation system.    Pumpless, fanless electrolyte-circulation system (10)    Electrolyzer core (12)    Water electrolyzer (14)    Electrolyte container (22)    Electrolytes (24)    Supply tube (26)    Return tube (28)
NOVELTY - Biogas to liquid fuel converter comprises a gas cleaning system having a condensate separation vessel (20) configured to remove moisture from a gas, and a polypropylene filter to remove particles, a syngas production system configured to receive the gas from the gas cleansing system, where the syngas production system has a catalyst configured to produce hydrogen and carbon monoxide and a flash tank to condense methanol from the gas, and a methanol synthesis system having a methanol synthesis reactor having catalysts to react with the gas at a temperature and a pressure to produce methanol.    USE - The biogas to liquid fuel converter is useful for making a liquid fuel, where the gas is a landfill gas or a sewage digester gas (all claimed) and the liquid fuel is methanol.    ADVANTAGE - The biogas to liquid fuel converter cleans and converts bio-gas into liquid methanol at much lower temperature and pressure with less water energy consumption.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a gas cleaning system.    Condensate separation vessel (20)    Gas booster (60)    Gas inlet (70)    Gas outlet (75)    Gas reheater. (80)
NOVELTY - Reducing (P1) total acid number (TAN) of a feedstock involves contacting an initial feedstock containing at least 60 wt.% bio-oil with an active ion exchange resin to provide a treated feedstock and an acid-enriched ion exchange resin, where at least 70 wt.% of the initial feedstock is recovered as the treated feedstock, where the treated feedstock has a TAN value that is at least 30% lower than the TAN value of the initial feedstock, where the treated feedstock has a carboxylic acid content that is at least 50% lower than the carboxylic acid content of the initial feedstock.    USE - For reducing total acid number (TAN) of a feedstock (claimed) such as bio-oil, useful for processing existing refinery equipment.    ADVANTAGE - The process effectively removes undesirable acidic components from the bio-oil, but does not negatively impact bio-oil yield at the same time. The ion exchange resin selectively removes at least a portion of the carboxylic acids from the bio-oil, while leaving most of the phenolic compounds in the bio-oil, which minimizes the overall impact on bio-oil yield; and reduces acidity and corrosiveness of the bio-oil, thus enhances its ability to be transported to and refined in conventional refineries. The process selectively removes at least a portion of the carboxylic acids, thus enhances stability and processability of the bio-oil.
NOVELTY - Selecting clones of microbial strains or animal cells, which are placed under induction conditions for producing proteins with a continuous supply of a solution containing compounds including at least one carbon-containing substrate, at least one nitrogen-containing compound and one or more mineral salts, is claimed, where the composition of the solution is chosen such that the elements of the compounds are present in a stoichiometric proportion to the composition of the expected product. The compounds are present in the form such that a pH-value is constantly maintained without regulation.    USE - The method is useful for selecting clones of microbial strains or animal cells, where the strains are useful for the production of recombinant proteins and enzymes from filamentous fungi, the enzymes are useful for the production of ethanol from lignocellulosic biomass, and the strains consist of genera Trichoderma, Aspergillus, Penicillium, Schizophyllum, Clostridium, and Trichoderma reesei (all claimed).    ADVANTAGE - The method allows the selection of clones of microbial strains or animal cells with high screening performance.
NOVELTY - Treating a subterranean formation to convert coal to methane, comprises: (a) introducing a solution containing at least one of an oxoacid ester of phosphorus or a thioacid ester of phosphorus into the subterranean formation; and (b) introducing at least one other chemical compound/chemical entity comprising hydrogen, carboxylic acids or their esters or salts, oxoacids of phosphorus or their salts, vitamins, minerals, mineral salts, metals or yeast extracts into the subterranean formation.    USE - The method is useful for treating a subterranean formation to convert coal to methane.    ADVANTAGE - The method increases the susceptibility (by way of chemical break down or solubilization) of large carbonaceous molecules (e.g. coal).
NOVELTY - Increasing (M1) saccharification efficiency of biomass comprises treating a chaperone protein and saccharogenic enzyme or saccharogenic enzyme composition together to biomass.    USE - The methods are useful for: increasing saccharification efficiency of biomass; and mass-production of bioethanol from biomass, where the biomass includes cellulose (all claimed).    ADVANTAGE - The method: prevents cellulase from losing its activity throughout the whole saccharification process, thus increasing glucose yield from plant biomass containing cellulose; and efficiently increases saccharification of biomass in an economic manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for mass-production (M2) of bioethanol from biomass, comprising: (a) inducing saccharification of biomass by treating the chaperone protein and saccharogenic enzyme or saccharogenic enzyme composition together to biomass; and (b) producing ethanol by alcohol-fermenting monosaccharides generated by the saccharification of step (a).
NOVELTY - An aqueous solution containing an inorganic acid metal salt and/or a metal hydroxide as a solute, is electrolyzed to generate hydrogen gas. The generated hydrogen gas is washed with water and passes through a mist filter. Trichlorosilane is reduced using the generated hydrogen gas, to precipitate polycrystalline silicon.    USE - Manufacture of polycrystalline silicon used for semiconductor devices.    ADVANTAGE - The polycrystalline silicon is manufactured stably with high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen gas.
NOVELTY - The system (10A) has a biomass gasifier (12) gasifying biomass (11). A gas cooler (14) cools generated gas from the biomass gasifier. A gas-purification apparatus (15) removes dust in the generated gas after cooling. A vapor supply line (L11) supplies vapor to the gas cooler from exterior. A vapor introduction line (L12) introduces high temperature vapor cooled by generated gas with the gas cooler and obtained by heat exchange as a gasifying agent into the biomass gasifier. A booster pressure-rises the generated gas after the dust removal.    USE - Biomass fuel gasification system for use in a chemical product synthetic system (claimed) for gasifying biomass fuel i.e. methanol, generated from biomass e.g. farm products or by-product, timber and plant. Can also be used for gasifying biomass fuel generated from rice bran, wood chip and coppiced timber.    ADVANTAGE - The system allows the excessive high temperature vapor to be returned to a chemical processing plant of a supply source of low-temperature vapor while supplying the high temperature vapor obtained by gas cooling into the gasifier such that excessive high temperature vapor can be introduced and heat-exchanged to a heat exchanger, which reheats the generated gas when installing a modifier that modifies the gasifying gas, so that excessive vapor arising inside the system can be used effectively, thus improving thermal efficiency of the system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a chemical product synthetic system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a biomass fuel gasification system.'(Drawing includes non-English language text)'    Vapor supply lines (L11, L13)    Vapor introduction line (L12)    Biomass fuel gasification system (10A)    Gasifying biomass (11)    Biomass gasifier (12)    Gas cooler (14)    Gas-purification apparatus (15)
NOVELTY - The manufacturing method involves arranging the fuel electrode (2B) and fuel generation member (1) of solid oxide fuel cell (2) inside, and forming space which can distribute gas between inside and exterior. The reducible gas is flowed in the space using the gas distribution unit, and an electrically-conductive material included in the fuel electrode is restored after the formation process. The gas distribution unit is closed, and the space is made into closed space after the restoration process.    USE - Manufacturing method for fuel cell system.    ADVANTAGE - Improves the yield since the lack of restoration of electrically-conductive material included in a fuel electrode can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell system. (Drawing includes non-English language text).    Fuel generation member (1)    Solid oxide fuel cell (2)    Fuel electrode (2B)    First piping (4)    First valve (5)
NOVELTY - This utility model claims a floor the marsh gas pool, the above ground pool marsh gas fermentation tank, comprising a cylindrical bottom of the fermentation tank is connected with the base of the ladder shape, the two ends of the base is bent upwards bending angle is 10 to 30 degrees. This utility model Overground fermentation cylinder for marsh gas tank, the fermentation tank is set with the sledge type skateboard on the base, makes it possible to easily fast by manpower or mechanism to move position of the marsh gas tank so as to pressure free movable biogas tank, which meets the different needs of the user, and the operation is simple and convenient. This utility model Overground fermentation cylinder for marsh gas tank, a simple improvement, convenient use and strong practicability.
NOVELTY - The utility model claims a kind of large straw marsh gas automatic production device, it comprises an adjusting pool, a screw rod feeding pump, an electric valve, a tank top thermometer, pressure gauge, radar material level meter, a heat preservation tray, a fermentation tank, a tank bottom thermometer, hot water circulating pump, a water source heat pump and the water thermometer, the adjusting pool, a screw rod feeding pump, an electric valve and the fermentation tank are connected in turn, the top end part of the two sides of the upper end of the fermentation tank is provided with a tank body pressure gauge and radar material level meter, the upper part of the fermentation tank is set on one side of the tank top thermometer, the lower part of the fermentation tank is set on one side of the bottom of the tank thermometer, the bottom of the adjusting tank (1) with one end of the hot water circulating pump is connected with the fermentation tank is further provided with a control pipe heat preservation tray fermentation tank, the hot water circulating pump is connected with the other end of the water thermometer, a water source heat pump. This utility model solves the problem that each link in the marsh gas production of the automatic control and realizes the automation of the marsh gas production process, improves the large marsh gas production;
NOVELTY - Using solar energy to marsh gas pool heating device system, comprising a multi-circulation heat exchange system, wherein a circulation water outlet pipe of solar energy heat collector box, a heat collector, an insulating water tank, a heat collector circulation water inlet pipe, a heat power machine for combining and exchanging system is connected with the circulating heat exchange system of solar energy and heat preservation water tank; the other one is composed of heat preservation water tank, a methane tank circulate a water inlet pipe, a thermal circulation coil pipe, marsh gas pool circulating water outlet pipe, pipeline cycle power system is connected with the circulating heat exchange system for heat preservation water tank and the marsh gas pool is composed of the thermal circulation coil pipe spiral is set on the marsh gas tank. This utility model can make the temperature in the marsh gas tank, and the temperature control in the optimal range, the high speed bacterial fermentation, improves the yield, especially in winter to marsh gas pool heating the methane tank to normal gas, improves the utilization rate and strong practicability.
NOVELTY - This utility model claims a belt drying bed layer of the marsh gas tank, comprising a tank body with an inner cavity, wherein the upper part of the inner cavity of the tank body is the lower part of the inner cavity of the air storage chamber, the tank body is fermentation chamber, the upper part of the pool body is provided with a fermentation chamber and a discharge port of the feed pipe, the top of the tank body is provided with an air storage chamber is connected with a gas-guide tube, gas storage chamber for a steam drying bed, the drying bed layer absorbs the water vapour in the marsh gas to avoid the steam corrosion of metal pipeline and metal device of marsh gas, improve the purity of the marsh gas and heat energy conversion rate, in addition, drying bed layer is set on the marsh gas tank, marsh gas pool to ferment to produce marsh gas after removing water by drying bed layer, there is no need to set a steam-water separator, a low cost and is convenient to popularize and apply.
NOVELTY - A phosphorus-recovered material contains mixture of coal ash, plaster, and alkaline solution.    USE - A phosphorus-recovered material for fertilizer manufacture (claimed).    ADVANTAGE - Phosphorus recovery performance is improved while suppressing high alkalinity of solution containing phosphorus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) phosphorus collection method which involves producing mixture of coal ash, plaster, and alkaline solution and adsorbing phosphorus by performing predetermined time water flow of solution which includes predetermined time immersion in solution containing phosphorus for the mixture; and    (2) manufacture of fertilizer which involves rubbing off or grinding outer surface of phosphorus-recovered material.
NOVELTY - Bioethanol is brewed by performing fermentation of by-product of raw sugar production and yeast.    USE - Bioethanol brewing for activation of methane fermentation (claimed).    ADVANTAGE - Recyclable food source can be positively utilized, clean energy can be produced, serious energy supply problem of country can be addressed, and greenhouse gas reduction, expansion of environmental industry, and development of fossil energy product and techniques can be achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for activation of methane fermentation which involves using hydrogen and carbon dioxide derived from bioethanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of bioethanol manufacture. (Drawing includes non-English language text).
NOVELTY - A methane-fermentation-gas purification system (1) consists of a digester (2) for decomposing organic waste into water and methane fermentation gas, a gas-purification unit (7) for purifying methane-fermentation gas by removing carbon dioxide from the gas, and a heater for heating the digester by using methane gas contained in the purification exhaust gas as fuel.    USE - System is used for purifying methane-fermentation gas (claimed).    ADVANTAGE - The system enables efficient purification of methane-fermentation gas and complete recycle of all methane gas obtained from organic waste. The digester can be controlled to run stably always.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane-fermentation-gas purification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the structure of methane-fermentation gas-purification system. (Drawing includes non-English language text)    Methane-fermentation gas-purification system (1)    Digester (2)    Gas-purification unit (7)    Boiler (8)    Controller (9)
NOVELTY - Obtaining a gaseous stream involves contacting a stream of humid air on the surface of a solid layer and a surface catalyst caused by ionic aqueous metal electrodes energized with electric current; and passing through a semipermeable barrier where it reacts with the surface of ilmenite at a temperature of 12-80 degrees C and ambient pressure or vacuum, thus pressure resulting in a gas stream.    USE - The method or device is useful for obtaining gaseous stream; for producing gases such as ammonia, hydrogen, hydrocarbons, pure nitrogen, water vapor or other gas, preferably ammonia and hydrogen (all claimed); and for power generation.    ADVANTAGE - The method or device for obtaining gaseous stream is simple, environment-friendly, and saves significant energy cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for obtaining a gaseous stream containing ammonia, hydrogen and hydrocarbons, comprising a cylindrical tube positioned horizontally, with two openings opposite the smaller diameter, an anode wire is connected by a conductive wire, to the positive pole of the power source, and a cathode consisting of a winding, around the anode, connected to the negative pole of the power source, both immersed in an electrolyte fluid deposited at the bottom of the tube and covering the electrodes and a porous ceramic barrier near the opening.
NOVELTY - The utility model claims a kind of high effectively denitriding nitrogen-containing biological fluidized bed reactor, which is composed of aerobic reaction zone, the first-stage anaerobic reaction area, a secondary anaerobic reaction zone and settling zone, aerobic reaction zone in the first-stage anaerobic reaction area, two-stage anaerobic reaction area is set between the first-stage anaerobic reaction area, the settling zone is provided with two-stage anaerobic reaction area, aerobic reaction area is provided with a internal circulation denitrification lifting storage device (2), a pulse aeration system (1), a system I (3) is connected with the aerobic reaction zone through a pipeline, the first-stage anaerobic reaction area is provided with a three-phase separator I (5), a stainless steel water outlet hole plate (6), a bucket (7) and a gas guide tube I (8), a pulse water distributing system II (4) is connected with the first grade anaerobic reaction zone via pipeline, the anaerobic reaction area is provided with a three-phase separator II (9) and a gas guide tube II (10), settling zone is provided with a water outlet weir plate (11) and a water outlet pipe (12). This utility model is suitable for sewage with high load aerobic system and high-load biological nitrogen removal system, it can calculate a reaction volume according to the design requirement, adjusting the frame size.
NOVELTY - This utility model claims a micro-power micro-charge sewage treatment device, a water distribution room is provided with a reaction tank a, water distribution room are connected through pipe is connected with the reaction tank a; the reaction tank is connected with a water distribution chamber to charge water tank, water distribution room, pipe, a reaction tank and a water tank to form a water circulating loop, wherein the water circulation loop is provided with at least one metal cation capable of generating sewage to the charge device, the metal capable of continuous oxidation reaction by weak current, the pollutant completely decomposition, degradation, forming stable phosphate, inorganic salt and the complex deposition, are connected in parallel or series connection device for processing different from the water, water quality, water quality can reach the discharge, there is no need to discharge organic sludge, sludge to overcome the problem, a low energy consumption when the harmless, purifying, clean and environment-friendly energy-saving.
NOVELTY - This utility model claims a kind of wind-light complementary aeration sewage treatment system. Wind-light complementary-aeration waste disposal plant complementary power generation aeration system is composed of a water inlet system, artificial floating island sewage treatment system and drainage system. A wind-light complementary aeration sewage treatment device is provided with a wind-light complementary generating device, the bottom wind-solar hybrid generating aeration is provided with aeration pump is connected with the aeration pipe, sewage treatment section artificial floating island is provided with foam plate with the thickness of 5 cm This utility model is a sewage treatment device, a wind-light complementation aeration technology, using the inexhaustible solar energy and wind energy aeration pump as the power source, the solar and wind energy providing clean, free of the electric energy, solar energy and wind energy at the same time can be complementary, and has very strong practicability and popularization value is common for oxygen aeration pump.
NOVELTY - A kind of straw percolating a solution device belongs to the field of agricultural production field, comprising a collecting barrel, a filter barrel, a nozzle, a return pipe, a rotary joint, a support frame and a pump, a filter barrel is put in the collecting barrel, the water surface of the filter barrel is opened with a small hole, and the upper end is provided with an outer edge, the outer edge can be placed on the upper end face of the collecting barrel, the bottom of the collecting barrel and filter barrel provided with a certain distance, the inlet end of the pump is connected with the collecting barrel is connected with the bottom, and the outlet is connected with return pipe of the pump, a return pipe are fixed together by the supporting frame and the collecting barrel, is provided with a rotary joint on the upper part of the return pipe, spray head is installed on the return pipe. Straw is installed on the filter barrel, the pump for collecting liquid draw onto the bottom of the barrel, the straw through the spray head, and then the liquid and flow into the collecting barrel through the small holes on the water filter barrel, so as to form a circulation, improves the microbial fermentation for oxygen and nutrient condition and greatly enhances the degradation of microorganism, so as to effectively improve the degradation efficiency of the straw.
NOVELTY - The utility model claims a fertilizer production device, specifically a kind of microorganism bacterial liquid fermentation tank, comprising a tank body, a heat pipe connected to the feeding pipe and the air pipe in the tank body, the other end with an observation port is set on the upper part of the tank body, wherein the tank body comprises an inner layer wall and the outer layer tank wall covered on the inner layer tank wall outer side of the heating pipe is located at the outer layer and the inner layer tank wall and tank wall, around the inner layer tank wall because of adopting said structure, this utility model is the microorganism bacteria liquid fermentation with adjustable height according to the number of the discharge, is more convenient and is not used, it can adjusted to the lowest part, it does not need large space, and the reaction is more complete, it has simple structure and convenient use.
NOVELTY - This utility model claims a biogas slurry stirring device, belonging to the production field of marsh gas, comprising a rocking handle, a steel sleeve, a bearing, a stirring shaft, a blade, spoon-shaped, steel ball, a base and a marsh gas tank, is installed on the top end of the stirring shaft, the steel ball is set with the bottom of the spoon-shaped paddle on the stirring shaft is welded on the stirring shaft, the blade is welded on the stirring shaft, the blade is set with the spoon-shaped blade above the marsh gas tank is poured base, a steel ball matched with the base is fixed on the upper part of the marsh gas tank, the steel sleeve, a stirring shaft and a steel sleeve through the bearing, the steel sleeve and the stirring shaft and a soft rubber elastic sealing ring, the whole device is set on the marsh gas pool, and biogas tank stirring shaft and the centre is 30 degrees. By the rocker crank handle drives the blade and a spoon-shaped paddle rotation, capable of effectively broken crust, spoon-shaped paddle of the marsh gas tank upper layer can fully stirring the supernatant layer, an active layer and a sediment layer, the third layer is capable of stirring together and improves production rate and gas production rate.
NOVELTY - This utility model claims a kind of straw for marsh gas tank, marsh gas tank, the middle part is provided with an adjusting wheel, an adjusting wheel is connected with the adjusting rod, the outer marsh gas tank is provided with a supporting wheel, the conveying belt is set with straw slot and the adjusting wheel, a supporting wheel, a supporting wheel is installed on one side of handle, the marsh gas tank can be directly using crop straw as raw material, feeding material, and continuously feeding and discharging, balance, floating will not crust.
NOVELTY - This utility model claims a high-efficient two-phase anaerobic fermentation device, comprising a hydrolysis acid production reactor, high temperature hydrolyzing device, at least one of methane production reactor, the bottom of the hydrolysis acid generating reactor penetrating fluid storage chamber and the methane generating reactor is connected, a hydrolysis acid generating reactor is set with hole connected with hollow stainless steel cone bracket, the conical bottom of the bracket with the high temperature hydrolyzing device methane reactor is provided with an upper and a lower material outlet, the upper part of the feed to form a self-circulation pipeline, a hydrolysis acid generating reactor component is connected with the rotating spray head, high temperature hydrolyzing device receives large particle solid conical support, and carrying out solid-liquid separation with press filter residue at the outlet. The device for processing process is simple, the structure is rational, and it is easy to maintain, the fermentation efficiency is high, the performance is stable and reliable, is suitable for anaerobic digestion treatment of organic waste, it can satisfy the mass production.
NOVELTY - A kind of hydraulic cyclone flow anaerobic digestion tower, the centre of the tower body is provided with a guide cylinder, the guide cylinder in the middle lower part of the cylinder is provided with a submersible motor, submersible motor is connected with the lifting impeller, the guide cylinder is connected with a guide pipe, the guide pipe and the upper-layer tower body is provided with a circle of annular constant-current plate, the side wall of the tower body is provided with a connected outside and the guide cylinder of the feeding pipe, the bottom of the tower body connected with slag hopper, the slag collecting bucket connected with discharging pipe, the top of the tower body is provided with a marsh gas pipe, a marsh gas pipe with the pressure transducer and an electric control box; This utility model use hydraulic rotational flow method to realize material stirring, slag breaking, raw clinker separating and improve anaerobic digestion treatment efficiency, improve the output and save anaerobic digestion process energy consumption, and a variable-strength anaerobic digestion technology to marsh gas, the marsh gas production system automatic operation. It can be widely applied to waste water, waste liquid, garbage, excrement, sludge and so on high thickness organic waste anaerobic digestion process.
NOVELTY - Electrolyte water electrolysis hydrogen production system, referring to the water electrolysis hydrogen manufacturing technology of self-circulation. This utility model comprises an oxygen separator, a hydrogen separator, an electrolytic bath, separately provided with a heat exchange pipe in the oxygen separator and the hydrogen separator are respectively connected with the first oxygen electrolyte mixed outlet pipe on one side of the electrolytic cell, a hydrogen electrolyte mixed outlet pipe, are respectively connected with the second oxygen electrolyte mixed outlet pipe on the other side of the electrolytic cell, a hydrogen electrolyte mixed outlet pipe are respectively connected with a return pipe and a return pipe at the two sides of the electrolytic cell, and the third return pipe is at lower side in the electrolytic cell, electrolytic bath is provided with several electrolytic cell is provided with a cell chamber are respectively connected with corresponding to the small holes on the tube body of the third return pipe. The utility model structure is more reasonable and simple, error is reduced, power consumption is reduced, the system works more stable and maintenance is more convenient, which greatly improves the whole reliability.
NOVELTY - This utility model claims a kind of used for treating domestic garbage, belonging to the domestic garbage treatment technology field. The system comprises a device for reflecting and accumulating solar radiation to a point or a zone, heating body, the sunshine focusing part is installed on the reflecting and accumulating device, and focusing the solar energy is used for heating the fluid in the heating body, a fermenting tank for domestic garbage for fermentation, and the fluid is heated in the heated body into the fermentation tank to ferment to generate marsh gas. This utility model solar energy obtained by use of reflecting and accumulating device, and the solar energy is used for heating the liquid in the heated body, the fluid for heating the fermentation tank to generate marsh gas, makes full use of the solar energy so as to save energy and improve the economic benefit.
NOVELTY - The method involves controlling inflow ammonia nitrogen concentration at 300-500 mg/L. Aeration quantity is controlled so that the concentration of dissolved oxygen is 0.2-0.5 mg/L. Aeration time is controlled so that ammoxidation rate is controlled at 30-50%. Sodium hydrogen carbonate is added to regulate and control pH at 7.70-8.20. Outflow nitrosation rate is calculated. The nitrosation rate is reached more than 90% after 4 days and 8 cycles, and the nitrosation rate is always more than 90% after 7 days and 14 cycles, so that the nitrosation is successively started.    USE - Sequencing batch reactor (SBR) nitrosation quick start method for urban sewage treatment and resource recycling.    ADVANTAGE - The nitrite after starting the sludge in the ammonia nitrogen concentration has the good stability. The processing efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the start stage nitrosation sludge process effect. (Drawing includes non-English language text)
NOVELTY - The method involves maintaining operation temperature of sludge in a SBR at low value of 11-16 degrees C. The water intake ammonia nitrogen concentration is 50+/-5 mg/L. The dissolved oxygen is maintained at 0.5-2.0 mg/L by controlling the aeration rate. The ammonia oxidation rate is maintained at 85-99% by controlling the aeration time. Sodium bicarbonate is fed to control the pH of inlet water at 7.65-8.20. The sub-efficiency is maintained over 90% at all times after 90 cycles of operation in 45 days. Stable operation is achieved in achievement of nitrosation.    USE - Method for nitrosation and stable operation of low-temperature and low-ammonia nitrogen sequencing batch reactor (SBR) for municipal sewage treatment and reclamation purpose.    ADVANTAGE - Stable operation of SBR nitrosation under low-temperature and low-ammonia nitrogen conditions is achieved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating stable operation of SBR.(Drawing includes non-English language text)
NOVELTY - Preparation of ritodrine hydrochloride comprises mixing 2-amino-1-(4-hydroxyphenyl) propanol hydrochloride and 4-ethylphenol at molar ratio of 1:1-2, and carrying out condensation reaction with added catalyst at 0-120 degrees C.    USE - Method for preparing ritodrine hydrochloride (claimed).    ADVANTAGE - The method has controlled production cost with improved product quality.
NOVELTY - Extracting and purifying Rehmannia root saponin involves: taking seed or leaf of the radix Rehmannia as raw material, crushing it, degreasing by using ether solvent, mixing the degreasing powder with alcohol-water mixed solution, extracting, decompressing and recycling alcohol, to obtain saponin crude product, subjecting obtained product to resin column purification, sequentially washing with distilled water, 10-40% alcohol solvent and 40-80% alcohol solvent, collecting 40-80% alcohol eluent, decompressing, distilling, re-crystallizing, and drying to form target product.    USE - For extracting and purifying Rehmannia root saponin (claimed).    ADVANTAGE - The present method is suitable for mass production; uses raw material which is easy to obtain; is simple and environment friendly; has low cost; and obtaining target product purity reaches more than 50% and yield more than 1.5%.    DETAILED DESCRIPTION - Extracting and purifying Rehmannia root saponin involves: taking seed or leaf of the radix Rehmannia as raw material, crushing it, degreasing by using ether solvent, mixing the degreasing powder with alcohol-water mixed solution, extracting, decompressing and recycling alcohol, to obtain saponin crude product, subjecting it to resin column purification, sequentially washing with distilled water, 10-40% alcohol solvent and 40-80% alcohol solvent, collecting 40-80% alcohol eluent, decompressing and distilling to remove the solvent to obtain the eluate, and re-crystallizing it, and then drying in a vacuum drying box to obtain the target product.
NOVELTY - The device has movable joint (15) whose lower end is connected to water cooling sleeve (16). Upper water cooling sleeve is fixed on rigid alundum tube (31) through a locator (22). The rigid alundum tube is vertically arranged on depositing furnace main portion (33), and temperature control cabinet (34) is connected with depositing furnace main portion. Thermoelectric coupler (32) is coupled to depositing furnace main portion whose lower end is connected with receiver (48) that is connected with water-cooling sleeve (35).    USE - Experiment device used for coal and biomass pyrolysis test.    ADVANTAGE - The device is featured with accurate control, wide temperature range, material staying time range is wide and operation is simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the experiment device used for coal and biomass pyrolysis test.    Movable joint (15)    Water-cooling sleeves (16,35)    Locator (22)    Rigid alundum tube (31)    Thermoelectric coupler (32)    Depositing furnace main portion (33)    Temperature control cabinet (34)    Receiver (48)
NOVELTY - This utility model claims a biogas with spraying device for mushroom planting basin, belonging to the technical field of new energy application biogas slurry, comprising a planting groove, planting groove is provided with an arc fixed, is fixed on the shed is provided with biogas slurry spraying device. Biogas slurry entering from the inlet of the biogas tank, filtering the residue by screen, the biogas slurry pipe flows to the spray head, the sealed cap, which avoids leakage, starting pressing device, a biogas tank and a biogas pipe, the biogas slurry is sprayed on the mushroom in planting groove from the spraying head, the spraying action, the utility model is added with biogas slurry spraying device, it only needs to start pressing device, it can realize automatic spraying biogas slurry of the mushroom in planting groove to realize the automatic spraying, is very convenient, reduces the labour cost and reduces the workload.
NOVELTY - This utility model claims a kind of marsh gas pool heat preservation heat insulation device, an anaerobic tank is provided with infrastructure layer under the ground, outside the anaerobic tank, the anaerobic tank outer wall and the infrastructure layer is provided with peripheral air heat insulation layer, the air heat-insulating layer is installed on the upper end of the cover plate, the cover plate is covered on the upper end of the pool wall and infrastructure layer, the upper part of the gas storage cabinet and the cover plate is equipped with a solar heating heat preservation chamber. The utility model ensures the four seasons marsh gas tank constant temperature operation, low operation cost, fermenting completely, the material utilization rate is high, the gas flow.
NOVELTY - The apparatus (1) has a modifier (7) which generates a hydrogen-containing-gas by reforming reaction of source gas and water. The removal devices (8,9) remove the mixture of carbon monoxide in hydrogen-containing-gas to react with reactive gas. A controller (18) controls the amount of raw material gas supplied by raw material suppliers (13,14) and controls the amount of oxidant gas supplied, on the basis of measured raw material gas flow rate measured by a measurement device (12) during the same period.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The hydrogen generating apparatus can effectively reduce carbon monoxide in hydrogen-containing-gas, even if the composition of source gas changes. The supply amount of modification water, combustion air, and oxidizing agent gas is accurately controlled. Since the hydrogen-containing-gas of predetermined amount is stably supplied to the fuel cell, the situation of fall and power generation stop of the electric power generation efficiency of the fuel cell can be prevented.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell system; and    (2) an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus.(Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Modifier (7)    Removal devices (8,9)    Measurement device (12)    Raw material suppliers (13,14)    Controller (18)
NOVELTY - A fluid containing fluoroolefin and alkane having one carbon number in which at least one hydrogen atom is optionally substituted with chlorine atom or fluorine atom is contacted, with synthetic zeolite 4A to remove alkane having one carbon number. Thus, the fluoroolefin is purified.    USE - Purification of fluoroolefin used in manufacture of 2,3,3,3-tetrafluoropropene, hexafluoropropene, 1,2,3,3,3-pentafluoropropene, 1,1,3,3,3-pentafluoropropene, 2,3,3,3-tetrafluoropropene, 3,3,3-trifluoropropene, tetrafluoroethylene, trifluoroethylene, 1,1-difluoroethylene, chlorotrifluoroethylene and 1-chloro-2,2-difluoroethylene (all claimed).    ADVANTAGE - The method provides fluoroolefin having high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of fluoroolefin; and    (2) manufacture of 2,3,3,3-tetrafluoropropene, which involves carrying out synthesis reaction with thermal decomposition of composition containing chlorodifluoromethane and a in presence of thermal medium.
NOVELTY - Method for producing organic acid, involves (a) crushing a lignocellulosic biomass containing cellulose, (b) washing the crushed product obtained in step (a) by water and (c) obtaining a saccharified product from the solid obtained in step (b) using hydrolase and (d) fermenting the saccharified product obtained in step (c) by filamentous fungi and obtaining organic acid.    USE - The method is useful for producing organic acid. The organic acid is lactic acid or fumaric acid (claimed). The method is also useful for biorefinery for producing biofuel.    ADVANTAGE - The method simply and safely produces organic acid. The organic acid removes fermentation inhibitors, inhibits decline of conversion rate during fermentation process, and improves saccharification reaction.    DETAILED DESCRIPTION - Method for producing organic acid, involves (a) crushing a lignocellulosic biomass containing cellulose having a cellulose I degree of crystallization exceeding 30% and decreasing the cellulose I degree of crystallization to 0-30%, where degree of crystallization is calculated by using specific equation involving a predetermined parameters such as Ic, and Ia, where Ic is diffracted intensity of the lattice plane having lattice spacing of 22.4 nm in x-ray diffraction and Ia is diffracted intensity of the amorphous portion having lattice spacing of 27.3 nm, (b) washing the crushed product obtained in step (a) by water and (c) obtaining a saccharified product from the solid obtained in step (b) using hydrolase and (d) fermenting the saccharified product obtained in step (c) by filamentous fungi and obtaining organic acid.
NOVELTY - The apparatus (100) has a gas separator (120) that is provided into which condensed natural gas flows. A gas separator separates vapor stream separated in gas-liquid separator into primary and secondary vapor streams. A heat exchanger (130) condenses primary vapor stream separated in gas separator. One expander (140) expands primary vapor stream condensed in heat exchanger. Other expander (150) expands secondary vapor stream separated in gas separator. A distillation tower (160) is provided into which liquid stream, primary and secondary vapor streams are flowed in.    USE - Fractional distillation apparatus of natural gas such as methane collected from drilled gas well.    ADVANTAGE - The energy used in discriminating the natural gas can be reduced and the energy efficiency can be improved.    DETAILED DESCRIPTION - The liquid stream, primary and secondary vapor streams are flowed into distillation tower so as to divide into overhead vapor stream containing methane and component-reinforced lower stream. The heat exchanger is provided for exchanging heat between primary vapor stream and overhead vapor stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the natural gas fractional distillation apparatus.    Natural gas fractional distillation apparatus (100)    Gas separator (120)    Heat exchanger (130)    Expanders (140,150)    Distillation tower (160)
NOVELTY - This utility model claims a kind of organic garbage quick fermentation device, comprising a fermentation tank, wherein the fermentation tank comprises a tank body, a tank body top end is provided with a feeding port, a tank body is set at the bottom, the tank body is provided with a hot air device, the hot air device is provided with an air inlet and an air outlet, the air inlet is connected with air inlet pipe, the fast fermenting device further comprises a drying machine and a marsh gas furnace, wherein the drying machine comprises a shell, a right end is provided with a high temperature air inlet, the left end is provided with a waste heat air outlet, the waste heat air outlet is connected with the air inlet pipe, the marsh gas generated by the furnace cooler by warm-air in high temperature air inlet of the dryer. This utility model is composed of a fermentation tank, marsh gas furnace, dryer, recycling system of fermentation tank, so as to repeatedly and circularly;
NOVELTY - This utility model claims a filler for sewage treatment reaction device, comprising a shell body, the bottom of the shell body is provided with a water inlet, the upper part of the shell is provided with water outlet, wherein the shell is filled with filler, the inner part of the shell body is provided with an S-shaped baffle plate, and S-shaped baffle plate is provided with micro-pore. Compared with the traditional technology, this utility model increases the S-shaped baffle plate, the biological filler is effective control on the two sides of the reactor the sewage with the microorganism fully contact reaction, the organic impurities in the sewage fully decomposing;
NOVELTY - The two pool, a cement, metal, glass steel, plastic and so on in the first kind of material can be built a pool cover marsh gas pool, a pool, wherein a marsh gas pool as floating and sinking air cover, a floating and sinking gas cover made air hole, air floating and sinking to cover from a pool of marsh gas, marsh gas pool to another, a floating and sinking air cover is dipped in liquid between the two pools as movable baffle plate, the floating and sinking gas cover, air floating and sinking cover made of metal or glass fibre reinforced plastic.
NOVELTY - Distillers grains alkali-modified adsorption material has adsorption removal rate of about 90-99% and adsorption capacity of 500 mg/g on lead(II) ion, cadmium ion, mercuric ion, chromium (III) ion, hexavalent chromium ion, silver ion, cupric ion and zinc(II) ion in heavy metal wastewater.    USE - Distillers grains alkali-modified adsorption material is used for preparing fuel ethanol by fermentation (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of distillers grains alkali-modified adsorption material, which involves subjecting raw materials containing distillers grains to alkali addition, blending, microwave heating, liquid slag separation, washing and drying.
NOVELTY - A kind of capable of sorting, outputting useful material, at the same time, but also can utilize waste heat retting can maintain the marsh gas ferment efficient stable operation of the silent and an ozone-free and harmless of urban garbage digester. The digester at first to collect the garbage into the central part of the circular stack retting storehouse for retting, sterilizing after crushing, crushing after the garbage enter into suspension separating pool is difficult to degrade floater, suspended matter and precipitate recycling output for use, the rest is, liquefying a degradation of organic cleaning water or a same shower into the circle around the stack retting storehouse building, can use the retting waste heat to maintain the methane digestion high-efficient stable operation of the marsh gas fermenting tank, the material liquid after digestion and in the building to complete digestion with square big pool for circular main marsh gas fermenting tank outer four corners of the secondary marsh gas fermenting tank (1) (2), a sedimentation tank and a clear water tank, the marsh gas enter into the gas storage chamber for further use. A clear water from the clear water tank or directly into the suspension separating pool to be used circularly.
NOVELTY - This utility model relates to a kind of external circulation re-oxygenating ecological system of river comprehensive management system, wherein it comprises a water pump and a side is set on the bank of the river 6 external recycle ecological reoxygenation processor, the system adopts micro-computer control, through a water pump (1) for pumping the river sewage circulating pipeline (2), a circulating pipeline (2) is assigned to each cycle ecological reoxygenation processor (4), a bottom processor to control the water level of the reoxygenation terminal (3). The comprehensive treatment system maintenance and low running cost.
NOVELTY - This utility model claims a kind of high-concentration horizontal self-discharging marsh gas generating jar, it is composed of a pressure tank (1), horizontal marsh gas fermentation tank (6) and gas-holder tank (12), a pressure tank is the end of the tank is provided with a sand settling groove (19) and a stirring material of the stirrer (2), the outlet of the separating tank by the feeding box (4) is connected to sealed horizontal marsh gas fermentation tank (6), the fermentation tank is provided with a heating device, the outlet through with the rear part of the fermentation tank is isolated box (10) is connected to gas-holder tank (12), gas tank, air storage tank is provided with a cabinet (14), the gas-holder tank baffle hole (20), slag storage channel is connected with tank (17), the top part of the fermentation tank is set biogas outlet (5) is connected through the pipeline with the air storage cabinet (14). The device is a high concentration fermentation, the material thickness can reach more than 15%, is 2.5 times higher than low-concentration fermentation. Marsh gas tank is set with heat preservation is good for a horizontal underground, the energy consumption is low, and it can ensure the normal operation in north winter.
NOVELTY - Dryer with waste heat reused comprises a shell, where the shell is driven to turn by a gear box; pitched blades are arranged in the shell to promote the materials to turn; a blanking hopper is arranged above the right end of the shell; a high-temperature wind inlet is arranged in the middle of the right end of the shell; a waste heat wind outlet is arranged on the upper part of the left end of the shell and is connected with a hot wind emitting device via a blast pipe; and a discharge pipe which pitches downward is arranged on the lower part of the left end of the shell.    USE - The dryer is useful for promoting fermentation of organic waste.    ADVANTAGE - The dryer has the beneficial effects that the waste heat wind outlet of the dryer is connected with the hot wind emitting device via the blast pipe and the hot wind emitting device can be arranged in a fermentation tank; via dead weight of rubbish, domestic rubbish is promoted to be quickly fermented and decomposed by storing heavy pressure in the tank and adopting the hot wind emitting device for heating, thus reducing the fermentation time, shortening the fermentation period and accelerating domestic rubbish disposal speed; and the waste heat of the dryer is reused, thus not only saving energy but also reducing environmental pollution.
NOVELTY - Rapid fermentation equipment for organic garbage comprises a fermentation tank, where the fermentation tank comprises a tank body; a charge hole is arranged at the top end of the tank body; a discharging hole is arranged at the bottom end of the tank body; a hot air diffuser is arranged inside the tank body; an air inlet and an air outlet are arranged on the hot air diffuser; the air inlet is connected with an air inlet pipe; and a dryer and a methane furnace.    USE - Rapid fermentation equipment for organic garbage (claimed).    ADVANTAGE - By using the rapid fermentation equipment for organic garbage, a cyclic utilization system consisting of the fermentation tank, the methane furnace, the dryer and the fermentation tank is formed, so as to achieve repeated and cyclic comprehensive utilization.    DETAILED DESCRIPTION - Rapid fermentation equipment for organic garbage comprises a fermentation tank, where the fermentation tank comprises a tank body; a charge hole is arranged at the top end of the tank body; a discharging hole is arranged at the bottom end of the tank body; a hot air diffuser is arranged inside the tank body; an air inlet and an air outlet are arranged on the hot air diffuser; the air inlet is connected with an air inlet pipe; the rapid fermentation equipment also comprises a dryer and a methane furnace; the dryer comprises a shell; a high-temperature air inlet is arranged at the right end of the shell; an afterheat air outlet is arranged at the left end of the shell; the afterheat air outlet is connected with the air inlet pipe; and high-temperature air generated by the methane furnace in combustion is guided into the high-temperature air inlet of the dryer through a hot air pipe.
NOVELTY - The tank (1) has hot water circulator (2) that is arranged in case (10). A waste heat warming circulator (4) is arranged in tank portion (30) of cooling tank (3). The hot water circulator is provided with hot water inlet (20) and cold water outlet (21). The waste heat warming circulator is provided with hot water outlet (40) and cold water inlet (41). The hot water inlet is connected with hot water outlet by pipeline. The cold water outlet is connected with cold water inlet by pipeline. The hot water circulator and waste heat warming circulator are continuously bending steel tubes.    USE - Water circulation heating methane tank.    ADVANTAGE - The waste heat of waste hot materials can be utilized to accelerate decomposing of organic matters to promote methane to be generated quickly. The fuel coal consumption can be reduced while reducing the cost. The cooling of the cooling tank can be accelerated. The methane can be generated under the low temperature condition even when the temperature is lower through cold and heat exchange.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water circulation heating methane tank.    Methane tank (1)    Hot water circulator (2)    Cooling tank (3)    Waste heat warming circulator (4)    Case (10)    Hot water inlet (20)    Cold water outlet (21)    Tank portion (30)    Hot water outlet (40)    Cold water inlet (41)
NOVELTY - The method involves heating water in waste heat warming circulator (4), using waste heat material in cooling tank (3). The heated water is fed to a hot water circulator (2) by waste heat warming circulator via the hot water outlet (40), the pipeline and the hot water inlet (20). The methane tank (1) is heated through hot water by hot water circulator. The water in hot water circulator in process is cooled and entered the waste heat warming circulator via the cold water outlet (21), pipeline and cold water inlet (41).    USE - Water circulation heating method of methane tank.    ADVANTAGE - The organic substance is accelerated to be decomposed by afterheat of waste heat material, and rapid generation of methane is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane tank and cooling tank.    Methane tank (1)    Hot water circulator (2)    Cooling tank (3)    Waste heat warming circulator (4)    Hot water inlet (20)    Cold water outlet (21)    Hot water outlet (40)    Cold water inlet (41)
NOVELTY - The device has feeding pipe (10) and methane pipe opening (9) that are set on top of fermenting tank (11) whose bottom is set with slag drainage port (8) and liquid drainage pipe (3). Gravity material pushing device (6) is arranged in feeding pipe with material storage unit at upper portion. Slag retaining annular plate (14) is arranged on upper portion inside the tank, and connected with outlet of feeding pipe at upper end and inner wall of tank at lower end. Liquid-slag separation plate (16) is arranged on lower portion inside the tank, and connected with inner wall of tank.    USE - Straw methane fermentation device.    ADVANTAGE - The straws with large particles can be directly digested and the materials can be successfully fed and discharged. The energy consumption of the fermentation device can be reduced. The input-output ratio can be reduced.    DETAILED DESCRIPTION - The device has material storage unit, gravity material pushing device and control element that are arranged to form an automatic charging unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw methane fermentation device.    Liquid drainage pipe (3)    Gravity material pushing device (6)    Slag drainage port (8)    Methane pipe opening (9)    Feeding pipe (10)    Fermenting tank (11)    Slag retaining annular plate (14)    Liquid-slag separation plate (16)
NOVELTY - An aerobic phosphorus removal bacteria for purifying sewage, Acinetobacter sp. sunda1001 (CCTCC M 2011210), is new.    USE - The aerobic phosphorus removal bacteria are useful for purifying sewage by degrading inorganic phosphorus in the polluted water (all claimed).    ADVANTAGE - The strain has inorganic phosphorus removal ability of 20 mgP/h/g dry cell weight or higher.
NOVELTY - Anaerobic treatment method of kitchen garbage, involves (a) processing to-be-treated kitchen garbage to obtain dense slurry, and (b) anaerobically treating the dense slurry to obtain biogas liquid, biogas and sludge, where content of total solid in the dense slurry is 15-20%.    USE - Anaerobic treatment method of kitchen garbage (claimed).    ADVANTAGE - The method is stable, simple, easy to perform and cost-effective, and has short residence time. The devices involved in method are simple and easy to operate.
NOVELTY - Biogas composite material, comprises 70-80 kg excrements of livestock, 10-15 kg mushroom residues, 10 g biological bacteria and 5 kg biogas residue.    USE - As biogas composite material.    ADVANTAGE - The biogas composite material has long aerogenesis duration, high biogas production rate and speed. The decomposition of cellulose and hemicellulose can be promoted, hence the utilization ratio of material can be enhanced. The methane content in biogas is obviously increased. The biogas is convenient for industrialized production and transportation. The usage is convenient for the farmers. The raw materials are easy to be obtained. The rural pollution can be effectively solved. The waste can be comprehensively used.
NOVELTY - A cathode material comprises a substrate and nickel-cobalt-tungsten-copper-boron (Ni-Co-W-Cu-B) alloy plated layer on the substrate. The alloy plated layer comprises 26.5-36.6 mass% Ni, 6.6-9.2 mass% Co, 50.8-60.7 mass% W, 2.3-4.6 mass% Cu, and 0.8-2.4 mass% B.    USE - Cathode material used in producing hydrogen by photoelectrocatalytic decomposition of water (claimed).    ADVANTAGE - The cathode material is capable of achieving high hydrogen production rate and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the cathode material, comprising preparing plating solution comprising Ni, Co, W, Cu and B, and dipping substrate in the plating solution.
NOVELTY - A (1'R,4'S,5S,6S,8'R,10'E,12'S,13'S,14'E,20'S,24'S)-6-cyclohexyl-24'-hydroxy-12'-(((2R,4R,5S)-4-methoxy-5-(((2R,4R)-4-methoxy-6-methyl-5-oxooxan-2-yl)oxy)-6-methyloxan-2-yl)oxy)-5,11',13',22'-tetramethyl-3',7',19'-trioxaspiro(oxane-2,6'-tetracyclo(15.6.1.14,8.020,24)pentacosane)-10',14',16',22'-tetraene-2',21'-dione (A) is new.    USE - New cyclohexyl-hydroxy-(methoxy-methyl oxooxan-oxy-methyloxan-yl)oxy-tetramethyl-trioxaspiro(oxane-tetracyclo pentacosane)-tetraene-dione is used for preparing cyclohexyl-dihydroxy(methoxy-methyloxan-yl)oxy methoxy-methyloxan-yl oxy-hydroxy-tetramethyl-trioxaspiro (oxane-tetracyclo pentacosane)-tetraene-dione for manufacturing Selamectin (all claimed).    ADVANTAGE - The cyclohexyl-hydroxy-(methoxy-methyl oxooxan-oxy-methyloxan-yl)oxy-tetramethyl-trioxaspiro(oxane-tetracyclo pentacosane)-tetraene-dione has high yield, and is economical with reduced environmental pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of compound (A), which involves subjecting oxidation of (1'R,4'S,5S,6S,8'R,10'E,12'S,13'S,14'E,20'R,24'S)-6-cyclohexyl-21',24'-dihydroxy-12'-(((2R,4R,5S)-5-(((2S,4R,5S)-5-hydroxy-4-methoxy-6-methyloxan-2-yl)oxy)-4-methoxy-6-methyloxan-2-yl)oxy)-5,11',13',22'-tetramethyl-3',7',19'-trioxaspiro(oxane-2,6'-tetracyclo(15.6.1.14,8.020,24)pentacosane)-10',14',16',22'-tetraen-2'-one;    (2) (1'R,4'S,5S,6S,8'R,10'E,12'S,13'S,14'E,20'S,24'S)-6-cyclohexyl-12'-(((2R,4R,5S)-5-(((2R,4R)-5,5-dihydroxy-4-methoxy-6-methyloxan-2-yl)oxy)-4-methoxy-6-methyloxan-2-yl)oxy)-24'-hydroxy-5,11',13',22'-tetramethyl-3',7',19'-trioxaspiro(oxane-2,6'-tetracyclo(15.6.1.14,8.020,24)pentacosane)-10',14',16',22'-tetraene-2',21'-dione (B);    (3) preparation of compound (B), which involves converting (A) with nucleophilic reagent into compound (B); and    (4) usage of (A) and/or compound (B), which is used for preparing Selamectin.
NOVELTY - Method for producing alkaline fertilizer involves (a) mixing phosphate ore tailing or low-grade phosphate rock with insoluble potassium-containing rock in weight ratio of 1:0.4-0.9, and adding 3-8 %mass anthracite to the mixture, (b) drying and grinding the mixture, (c) preparing material block using powder obtained in step (b), (d) placing the prepared material block into kiln, roasting at 1000-1200 degrees C for 30-150 minutes to obtain sintered clinker, and (e) quenching the obtained sintered clinker using water, and draining, drying, crushing and grinding the product.    USE - The method is useful producing alkaline fertilizer (claimed).    ADVANTAGE - The method is simple, consumes low energy, and causes no pollution as it doesn't contain sulfur dioxide gas in tail gas.    DETAILED DESCRIPTION - Method for producing alkaline fertilizer involves (a) mixing phosphate ore tailing or low-grade phosphate rock with insoluble potassium-containing rock in weight ratio of 1:0.4-0.9, adding 3-8 %mass anthracite to the mixture, (b) drying and grinding the mixture to obtain powder, (c) preparing block material using powder obtained in step (b), (d) placing the prepared block material in kiln, roasting at 1000-1200 degrees C for 30-150 minutes to obtain sintered clinker, and (e) quenching the obtained sintered clinker using water to reduce the temperature to 400-700 degrees C, and draining the water, drying, crushing and grinding the product.
NOVELTY - The method involves providing aeration opening air compressor (10) for providing oxygen to sequencing batch reactor to convert nitrogen into nitrogen oxide according to output signal of process controller. The anoxic denitrification bacterium is used as ferment product for denitrification process. The phosphorus accumulating bacteria is taken as nitrogen oxide electron acceptor for denitrifying phosphorus. The sludge is entered into sequencing batch reactor from sludge storage tank. The discharging volume and sludge volume of reactor are same.    USE - Method for strengthening urban sewage nitrogen and phosphorus removal by sludge fermentation.    ADVANTAGE - The urban sewage nitrogen and phosphorus removal effect can be improved so that easily degradable carbon source generated by sewage fermentation can be consumed timely by phosphorus-accumulating bacterium and denitrifying bacterium. The nitrogen removal effect of the urban sewage with low carbon/nitrogen (C/N) ratio is enhanced. The problem of lowered fermentation reacting rate caused by accumulation of products in the fermentation process is avoided, and the initial stabilization of primary sludge is achieved.    DETAILED DESCRIPTION - The method involves opening water valve such that clear liquid is discharged into water tank (1). The anaerobic fermentation is performed for desired period of time. The nitrifying liquid in water tank is entered into sequencing batch reactor by water pump (5) and controlled by control switch. The air is entered into batch reactor through aerobic starting air inlet valve and water pump. The phosphate in the mixed solution is removed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for strengthening urban sewage nitrogen and phosphorus removal by sludge fermentation.    Water tank (1)    Water pump (5)    Air compressor (10)    Stirrer (12)    Temperature control device (20)
NOVELTY - Production of organic fertilizer comprises adding solid carbon, carbon removal algae and sewage waste with carbon (C), nitrogen (N) and phosphorus (P) to obtain compost raw material, adding additive, and fermenting; adding bacteria, heating, cooling by turning compost pile, and repeating steps three times; adding cultured earthworms, and watering daily to obtain vermicompost fertilizer granules; and recovering earthworms for animal protein processing, and recycling vermicompost for organic fertilizer processing.    USE - Production of organic fertilizer (claimed) used for soil maintenance.    ADVANTAGE - The method allows carbon dioxide to form the organic fertilizer, removes heavy metals, and increases organic matter content in soil.    DETAILED DESCRIPTION - Production of organic fertilizer comprises:    (A) composting solid carbon, carbon removal algae and sewage waste to obtain carbon (C), nitrogen (N) and phosphorus (P)sources with weight ratio of 100:5:1, adding additive at weight ratio of 100:3, and fermenting;    (B) adding 0.3 wt.% bacteria, heating to 60-70 degrees C, cooling by turning compost pile, and repeating steps three times;    (C) adding cultured earthworms at 15-35 degrees C, humidity of 40-90% and pH of 6-8.6, and watering daily to about 75% moisture content to obtain vermicompost fertilizer granules with 80-90% edible earthworm; and    (D) recovering earthworms for animal protein processing, and recycling for organic fertilizer processing.
NOVELTY - A pollution-free organic fertilizer is prepared by drying livestock manure and crop wastes, crushing, and adding into vertical open fermentation tank; adding microbial strain and controlling water content; mixing heat transfer fluid to mixed material, heating, maintaining heat, controlling fermenting temperature, intermittently stirring and mixing material, and fermenting; fully fermenting and decomposing, reducing moisture content, and feeding mixed material to aging tank; and aging mixed material and stacking, and carrying aeration and turning everyday.    USE - Method for preparing pollution-free organic fertilizer (claimed).    DETAILED DESCRIPTION - A pollution-free organic fertilizer is prepared by drying 70-85 wt.% livestock manure and 15-30 wt.% crop wastes, crushing, and adding into vertical open fermentation tank; adding 1-1.5 microbial strain/1000 mixed material and controlling water content at 60-65%; mixing heat transfer fluid at 90 degrees C to mixed material to ferment, heating to 70-75 degrees C, maintaining heat for 3 hours, controlling fermenting temperature, intermittently stirring and mixing material at 60-75 degrees C, and fermenting for 5-8 days; fully fermenting and decomposing, reducing moisture content to 30-35%, and feeding mixed material to aging tank; and aging mixed material and stacking for 15-20 days, and carrying aeration and turning everyday until temperature reduces to less than 40 degrees C.
NOVELTY - Natural biodegradable coated slow-release fertilizer is formed by wrapping a coating on the surface of granulated fertilizer, where the coating is waste edible mushroom cake of 5-50 wt.%.    USE - Natural biodegradable coated slow-release fertilizer.    ADVANTAGE - The fertilizer can be controlled to slowly release in the soil by adopting the coating material, and can be quickly biodegraded in the soil after the fertilizer is released completely in the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the coated slow-release fertilizer, which involves dissolving waste edible mushroom cake in ethanol/diethyl ether mixed solvent to prepare the coated liquid, coating the obtained liquid on the surface of the granular fertilizer, recycling the solvent and obtaining the coated slow-release fertilizer.
NOVELTY - An N-alkoxy-4-penten amide derivative (I) is new.    USE - New N-alkoxy-4-penten amide derivative used for preparing amide drug and as pyridone drug precursor (claimed).    ADVANTAGE - The method is simple and environmental-friendly and has large adjustable structure and low cost.    DETAILED DESCRIPTION - An N-alkoxy-4-penten amides derivative of formula (I) is new.    R=H, 1-6C alkyl, benzyl or aryl; and    R'=H or 1-4C hydrocarbon.    An INDEPENDENT CLAIM is included for the preparation of N-alkoxy-4-penten amide derivative.
NOVELTY - Crystallization of piperacillin comprises adding water into piperacillin, controlling at 5-10 degrees C, adding sodium bicarbonate to prepare pH value at 4.9-5.1, where concentration of piperacillin sodium aqueous solution is 10-50 wt.%, and absorbing piperacillin sodium solution by ETDA disodium salt and activated carbon and removing impurity, dividing into two phases after acidifying and crystallizing at 0-50 degrees C, filtering, washing and drying, where the first stage acid pH value of the crystal is 4-4.5, and the second stage acidifying and crystallizing pH value is 1-1.5.    USE - Method for crystallizing piperacillin (claimed).    ADVANTAGE - The method has easily obtained raw material, low cost and good product quality, and is environment-friendly and safe.
NOVELTY - Preparation of phosphatidylcholine comprises pulping the fresh chicken lung with deionized water by 200-mesh screen to obtain a slurry; carrying out enzymolysis by heating the slurry to 35 degrees C for 2-5 hours, and adding 1-5% of 1398 neutral protease; carrying out solvent extraction by pulping the enzymolysis liquid, cooling to room temperature, separating solvent layer to obtain lipids oil, and washing the lipids with acetone until there is no oil; and dissolving phosphatidylcholine in 95% ethanol at a weight-to-volume ratio of 1:4-1:8, and extracting using ethanol.    USE - Method for the preparation of phosphatidylcholine (claimed) used for pharmaceutical liposome processing.    ADVANTAGE - The method achieves more than 80% phosphatidylcholine. It reduces chicken processing waste and reduces environmental pollution, and achieves high-purity phosphatidylcholine products.    DETAILED DESCRIPTION - Preparation of phosphatidylcholine comprises processing fresh chicken lung by washing blood and impurities; pulping the fresh chicken lung with deionized water at a weight to volume ratio of 1:3-1:10, by 200-mesh screen to obtain a slurry; carrying out enzymolysis by heating the slurry to 35 degrees C for 2-5 hours, and adding 1-5% of 1398 neutral protease; carrying out solvent extraction by pulping the enzymolysis liquid, cooling to room temperature, where the volume ratio of enzymolysis liquid and the solvent of 1: 0.5-1:2, separating solvent layer to obtain lipids oil, and washing the lipids with acetone until there is no oil; and dissolving phosphatidylcholine in 95% ethanol at a weight-to-volume ratio of 1:4-1:8, and extracting using ethanol.
NOVELTY - A household garbage landfill biogas collection method is performed by using garbage layer hump ditch as horizontal well and high-density polyethylene (HDPE) pipe in which production of every 50 m of hump ditch is used for manufacturing vertical guide air well. Every horizontal well pipe of 100 m long is connected with branch pipe of 400 m long with angle of 60 degrees in which main pipe heads to 4% slope while branch pipe heads to 5% slope. Ladder-shaped square is placed above the horizontal well angle iron in which angle iron frame size has 0.6 m upper part, 1.6 m lower part, and height of 3 m.    USE - A household garbage landfill biogas collection method (claimed).    ADVANTAGE - Waste pile water content is reduced, and anaerobic degree around biogas collection wells, waste pile gas permeability, and biogas collection rate are improved.    DETAILED DESCRIPTION - A household garbage landfill biogas collection method is performed by using garbage layer hump ditch as horizontal well and high-density polyethylene (HDPE) pipe in which production of every 50 m of hump ditch is used for manufacturing vertical guide air well. Every horizontal well pipe of 100 m long is connected with branch pipe of 400 m long with angle of 60 degrees in which main pipe heads to 4% slope while branch pipe heads to 5% slope. Ladder-shaped square is placed above the horizontal well angle iron in which angle iron frame size has 0.6 m upper part, 1.6 m lower part, and height of 3 m. Iron wire plastic grid is welded into HDPE pipe and perforated with diameter of 300 mm on 2 sides of angle iron frame. HDPE pipe with steel wire is hung to ensure smooth slope of HDPE pipe to water guide pipe. Upper part of pipe is cover with gravel, and horizontal well is filled with gravel to cover garbage layer.
NOVELTY - A device for rapid enrichment multiplication and purifying culture of anaerobic ammonium oxidizing bacteria comprises water pre-heating system, trough, filter tank, bioreactor, inlet pipe, heating unit, temperature measurement mechanism, temperature control unit and peristaltic pump.    USE - The device is used for rapid enrichment multiplication and purifying culture of anaerobic ammonium oxidizing bacteria (claimed).    ADVANTAGE - The device and method can achieve rapid enrichment multiplication and purifying culture of anaerobic ammonium oxidizing bacteria so as to provide sufficient inoculated sludge for starting an anaerobic ammonia oxidation denitrifying reactor and achieve rapid start of the oxidation reactor to remove ammonia nitrogen and nitrite nitrogen out of wastewater.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for rapid enrichment multiplication and purifying culture of anaerobic ammonium oxidizing bacteria by arranging a device above; placing a certain amount of washed and filtered aerobic active sludge into a trench type biological reaction tank, and mixing the aerobic active sludge with a nutrient solution; gradually introducing the nutrient solution heated by a preheating system into the reaction tank; intercepting anaerobic ammonium oxidizing bacteria through cloth-type suspension fiber filler; and after 60-90 days culture, taking out the cloth-type suspension fiber filler full of brown anaerobic ammonium oxidizing bacteria, eluting and naturally precipitating to obtain a great amount of anaerobic ammonia oxidation denitrified sludge with high purity.
NOVELTY - Screening and domesticating composite microbial system for low-temperature degradation of straws comprises carrying out restrictive subculture preliminary screening, low-temperature gradient induced domestication and cellulase enzyme activity re-screening, and carrying out low-temperature multi-generation restrictive carbon source subculture domestication to obtain the composite microbial system for low-temperature degradation of straws.    USE - The method is used for screening and domesticating composite microbial system for low-temperature degradation of straws (claimed).    ADVANTAGE - The screening and domesticating method has high efficiency.    DETAILED DESCRIPTION - Screening and domesticating composite microbial system for low-temperature degradation of straws comprises acquiring a natural material sample rich in cellulose in an alpine area in which the annual average temperature is 0.6-8 degrees C, carrying out enrichment culture on a cellulose degradation microbial system, then carrying out restrictive subculture preliminary screening, low-temperature gradient induced domestication and cellulase enzyme activity re-screening, and then carrying out low-temperature multi-generation restrictive carbon source subculture domestication to obtain the composite microbial system for low-temperature degradation of straws.
NOVELTY - Automatic treatment of organic household garbage, involves: (A) crushing: separating and recycling the organic garbage from the household garbage, crushing the separated organic garbage by using a crusher and adding a fermentation aid into the organic garbage to be mixed; and (B) fermenting: conveying the mixed organic garbage and excrement drained from a closes tool into a marsh gas pond by using a drain pipe so as to be fermented, and conveying the marsh gas obtained by fermenting into a marsh gas generating set to perform power generating.    USE - Automatic treatment of organic household garbage (claimed).    ADVANTAGE - According to the method, the excrement, food residues from kitchens and other organic household garbage in the residential area are treated automatically and are converted into energy sources for the power supply of the residential area of people, so that the municipal construction investment of a city is saved and the environmental pollution is reduced. In addition, a new energy and a comprehensive utilization way are added.
NOVELTY - An electrochemical synergistic lignocellulose biodegradation, involves: hydrothermal pretreatment of raw material lignocellulose at 150-200 degrees C for 30-70 minutes; mixing the pretreated lignocellulose raw material and water solution with a strain for producing marsh gas by anaerobic fermentation; putting into an anaerobic fermentation bioreactor; and applying a voltage of 0.05-5 V to carry out anaerobic fermentation at 30-60 degrees CC under anaerobic conditions, continuous production of biogas.    USE - Electrochemical synergistic lignocellulose biodegradation (claimed).    ADVANTAGE - The method has good effect on degrading the lignocellulose raw material, and the quality of the produced marsh gas is high. It increases the fermentation speed and greatly enhances the biomass conversion rate, and the marsh liquid and marsh slag after fermentation can be used as an organic compound.    DETAILED DESCRIPTION - An electrochemical synergistic lignocellulose biodegradation, involves: hydrothermal pretreatment of raw material lignocellulose at 150-200 degrees C for 30-70 minutes; mixing the pretreated lignocellulose raw material and water solution with a strain for producing marsh gas by anaerobic fermentation; putting into an anaerobic fermentation bioreactor; and applying a voltage of 0.05-5 V to carry out anaerobic fermentation at 30-60 degrees CC under anaerobic conditions, continuous production of biogas, where the mixture for anaerobic methane fermentation contains an amount of a mixture of strains of 15-50 mass%, the mixture lignocellulosic feedstock mass of 10-35%, and the rest is water.
NOVELTY - Production of volatile short-chain organic acid involves pre-treating sludge as mode substrate using sodium hydroxide, centrifuging and removing supernatant as influent water of reactor, inoculating acid-producing seed sludge for anaerobic acid production reaction, and adding reduced amount of hydrated metal compounds to promote the growth and activity of an acid-producing bacterium group. The addition amount of hydrated metal compound is 1-300 mg/L or 1-3000 mg/L.    USE - Production of volatile short-chain organic acid (claimed).    ADVANTAGE - The method efficiently and economically provides volatile short-chain organic acid having high transformation rate.    DETAILED DESCRIPTION - Production of volatile short-chain organic acid involves pre-treating sludge as mode substrate using sodium hydroxide, centrifuging and removing supernatant as influent water of reactor, inoculating acid-producing seed sludge for anaerobic acid production reaction, and adding reduced amount of hydrated metal compounds to promote the growth and activity of an acid-producing bacterium group. The addition amount of hydrated metal compound is 1-300 mg/L or 1-3000 mg/L. The maximum output of the volatile short-chain organic acid is 0.32 gram per gram organic substances.
NOVELTY - The gasifier (1) has small-circle pipes that are provided to divide a horizontal type rotation cylinder (2) to thermal decomposition space (5) and discharge side space (6). The advancing direction of solid is made same or mutually opposed within a spiral cylinder (4). A water vapor feed pipe (9) is indirectly heated within horizontal type rotation cylinder, and is provided for feeding the raw material into thermal decomposition space. A heating unit is provided to supply heat to the inside of cylinder from the exterior through cylindrical side wall of rotation cylinder.    USE - Gasifier of organic waste such as garbage, paper and plastic and industrial waste such as woody biomass, mowed grass, pruned branch, waste plastic, construction waste material, animal-and- plant residue and sewage sludge.    ADVANTAGE - The gas and chemical materials such as energy fuel, electric power, vapor, hydrogen and alcohol can be produced efficiently and cleanly. Since the useful gas is produced from organic waste, the unit process cost and running cost can be reduced and the economical efficiency can be improved. Since the waste plastic containing halogen elements such as chloroethylene and electronic device substrate are changed into the useful gas by one unit process, the economic effect can be improved. The isolation storage of radioactive secondary waste can be performed easily, without incinerating the waste material. The volume of organic waster can be reduced. The safety and economical effect of gasifier can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasifier.    Gasifier (1)    Horizontal type rotation cylinder (2)    Spiral cylinder (4)    Thermal decomposition space (5)    Discharge side space (6)    Water vapor feed pipe (9)
NOVELTY - Manufacture of solid fuel involves baking wood-type biomass containing bark with size of 60 mm or less, and fraction having less than 0.5 mm-size of less than 10 %mass at 170-350 degrees C under oxygen concentration of 10% or less.    USE - Manufacture of solid fuel (claimed) used for power generation equipment and incineration system.    ADVANTAGE - The solid fuel has excellent grindability and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel.
NOVELTY - Method for recovering acid from sugar liquid, involves removing salt by adding alkali to the sugar liquid, depositing the salt, precipitating and separating solid and liquid, and recovering acid. The sugar liquid is obtained by adding acid to woody biomass, and hydrolyzing the cellulose and hemicellulose in woody biomass.    USE - The method is useful for recovering acid from sugar liquid (claimed).    ADVANTAGE - The method is flexible and cost-effective, enables to neutralize sugar liquid rapidly, and enables to utilize a cheap material for recovery apparatus.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing sugar liquid, involves adding acid to woody biomass, hydrolyzing cellulose and hemicellulose in woody biomass, adding alkali to the obtained sugar liquid, where salt is deposited, separating solid and liquid, and removing the depositing salt; and    (2) fermentation method, involves fermenting the sugar liquid.
NOVELTY - Method for manufacturing ethanol, involves pretreating wood biomass, saccharifying the product first time using enzyme, fermenting the product first time using ethanol, subjecting the product to mechanical treatment, saccharifying the product first time using enzyme, and fermenting the product first time using ethanol.    USE - The method is useful for manufacturing ethanol (claimed).    ADVANTAGE - The method improves saccharification yield and ethanol yield, can be prepared easily and inexpensively by utilizing reduced input energy.
NOVELTY - Electrochemical reformation of methane from its fumes, comprises coupling hydrogenation of carbon dioxide with the water electrolysis in a gas power plant, in a first phase of operation for natural gas or methane extraction from the gas grid, and combusting methane extraction to produce electrical energy, and discharging to the power supply, hydrogenating the carbon dioxide collected in the first operating phase using the hydrogen formed in the electrolysis of water to reform the methane, and introducing the methane gas into the network.    USE - The method is useful for electrochemical reformation of methane from its fumes.    ADVANTAGE - The method allows addition of higher doses of hydrogen and utilizes renewable energy sources for electrolysis.    DETAILED DESCRIPTION - Electrochemical reformation of methane from its fumes, comprises coupling hydrogenation of carbon dioxide with the water electrolysis in a gas power plant, in a first phase of operation for natural gas or methane extraction from the gas grid, and combusting methane extraction to produce electrical energy, and discharging to the power supply, where carbon dioxide is separated from fuel gases collected and stored and electrical energy is received from the power grid by the water electrolysis in a second operating phase, hydrogenating the carbon dioxide collected in the first operating phase using the hydrogen formed in the electrolysis of water to reform the methane, and introducing the methane gas into the network.
NOVELTY - This utility model claims a food fresh-keeping drying and integrated device, by making use of straw, the tail vegetables, organic matters such as sewage enters the biological energy producing area processing to generate marsh gas, organic fertilizer, liquid fertilizer, biological energy source. Intermittent food fresh-keeping drying for not only can realize keeping of fruit and vegetable is new picking fresh also capable of drying the vegetable and fruit is not sold out. Intermittent food fresh-keeping drying room for food fresh-keeping method for a plurality of food fresh-keeping a use marsh gas fresh-keeping, maintaining temperature by using ground water in it. Intermittent food fresh-keeping drying room for drying food using solar energy and marsh gas double-heat source providing heat to the food drying and automatic power control system according to the temperature, humidity sensor automatically controlling, keeping room temperature and humidity.
NOVELTY - This utility model claims a kind of LDIC anaerobic reactor, anaerobic reactor used for solving the problem of adequately high concentration waste water processing, the processing load is not high, comprising a reactor, comprising a reaction chamber having a cavity in the bottom of the reactor; settling chamber, is provided with a cavity on the upper part of the reaction chamber, through the first three-phase separator is connected with a reaction chamber, water outlet chamber, a third cavity on the upper part of the deposition chamber, through a three-phase separator is connected with a deposition chamber, water distributor is set at the bottom of the reaction chamber, a reaction chamber, a gas-liquid separator, air outlet is set on the upper part, the three-phase separator is respectively connected with the first and the second three-phase separator, wherein the top part is provided with a gas collecting pipe, a gas-liquid separator for separating liquid is sent to the content distributor, the water circulation device. The anaerobic reactor, treatment of organic waste water, the processing load is high, the purity of clean water and the separated biogas is high.
NOVELTY - Purification of biogas comprises adding water with humic acid powder uniformly stirring, slowly adding strong acid, uniformly stirring to obtain slurry, adding slurry to biogas liquid, uniformly stirring to react, standing, discharging purified biogas, and recycling.    USE - Method for purifying biogas (claimed).
NOVELTY - The system has a precise filter which is connected with a reaction tank (1). A clear liquid outlet end (3) is provided in the upper portion of a sedimentation tank (2). A sludge condensing tank (13) is connected to a filter (14) through a pump. Concentrated water storage tank (11) is connected to the liquid inlet end of a heater (12). Ion exchange unit is connected with the liquid outlet end of the precise filter. A liquid outlet is connected with one end of desorption liquid storage tank (8). An electro-dialysis device (10) is connected with the water storage tank.    USE - Guanidinium sewage processing system. Can also be used in processing medicine, pesticide and dye.    ADVANTAGE - The sewage processing system can be operated simply. The efficiency of the sewage processing system is high. Energy consumption of the processing system is low. The sewage processing system is environment friendly. The operation cost of the sewage processing system can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing guanidinium sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the guanidinium sewage processing system. (Drawing includes non-English language text)    Reaction tank (1)    Sedimentation tank (2)    Clear liquid outlet end (3)    Desorption liquid storage tank (8)    Electro-dialysis device (10)    Concentrated water storage tank (11)    Heater (12)    Sludge condensing tank (13)    Filter (14)
NOVELTY - Environment-friendly refrigerant comprises 1-4C hydrocarbon or fluorinated hydrocarbon with part of hydrogen atoms substituted by fluorine atoms, and 0.51-2.50 wt.% tetrahydrothiophene (THT).    USE - Environment-friendly refrigerant used for air conditioning device (claimed).    ADVANTAGE - The environment-friendly refrigerant has low greenhouse effect index and no special requirement on refrigeration devices and does not damage the ozone layer. When leakage occurs to the air conditioning device, the user can sense instantly and a timely measure can be taken. Thus, people's property safety is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for air conditioning device in which refrigerant is used.
NOVELTY - Method for enhancing soil fertility by prompting straw degradation with cellulase involves (a) crushing straw into length of 0.1-8 cm, (b) spraying cellulase solution on the crushed straw, and (c) embedding the processed straw in soil, where the method is implemented under a condition that the daily average temperature is 20-29 degrees C.    USE - The method is useful for enhancing soil fertility by prompting straw degradation with cellulase (claimed).    ADVANTAGE - The method enables to increase the decomposition rate of straw by using exogenous cellulase, changes waste into valuable product, thus relieves the pressure of straw burning on the environment, reduces soil damage with use of chemical fertilizers, increases the soil nutrients and promotes growth rate of crop.
NOVELTY - A fully water soluble nitrogen-phosphorus-potassium diverse defluorinated nitrofertilizer is produced by adding nitric acid phosphate solution; separating insoluble substance, freezing and crystallizing calcium nitrate, neutralizing, evaporating, granulating, drying and cooling. A mother liquor is added between calcium nitrate filtration and defluorination steps.    USE - Method for producing fully water soluble nitrogen-phosphorus-potassium diverse defluorinated nitrofertilizer (claimed).    ADVANTAGE - The method is able to recycle fluorine source to obtain potassium fluosilicate product, reduce fluorine to the environment, and avoid phosphate deposition.
NOVELTY - The marsh gas digester frame comprises a fermenting tank, and a pressing frame connected with an air outlet. The fermentation tank has an inner ring frame comprising annular concentric rings. The annular concentric rings are arranged and fixed to a column through a fixing rib socket. A top part of the fermentation tank is radially extended to a supporting top plate. The supporting top plate is welded on an inner ring. A pressure chamber frame comprises angle steels that are welded to each other, and is present in a cuboid structure.    USE - Used as a methane tank support frame.    ADVANTAGE - The methane tank support frame has simple structure, is convenient to use, and exhibits reduced labor consumption and improved corrosion and pressure resistances and stability.    DETAILED DESCRIPTION - The marsh gas digester frame comprises a fermenting tank, and a pressing frame connected with an air outlet. The fermentation tank has an inner ring frame comprising annular concentric rings. The annular concentric rings are arranged and fixed to a column through a fixing rib socket. A top part of the fermentation tank is radially extended to a supporting top plate. The supporting top plate is welded on an inner ring. A pressure chamber frame comprises angle steels that are welded to each other, and is present in a cuboid structure. A middle part of the pressure chamber frame is welded with a supporting frame. The fixed rib socket is fixed with the supporting frame by a bolt. The fermentation tank bracket supports a central upright post. The central upright post comprises a support base, and a support upright post. The supporting base is an annular structure, and is vertically fixed with the support upright post. An upper end of the supporting upright post is fixed on the top part of the fermentation tank. A cross section of the fermentation tank is arc vault structure.
NOVELTY - A biological agent composition for fermenting marsh gas, comprises: 2-5 wt.% alpha -amylase, 3-6 wt.% glucose amylase, 15-25 wt.% cellulose, 12-28 wt.% pectin enzyme, 15-25 wt.% neutral xylanase, 10-20 wt.% xylanase acid, 3-7 wt.% mannanase, 10-18 wt.% beta -dextranase, 25-35 wt.% Bacillus subtilis, 12-25 wt.% Aspergillus awamori, 10-25 wt.% Trichoderma koningii, 1-2 wt.% calcium carbonate and 1-2 wt.% urea.    USE - As biological agent composition for fermenting marsh gas useful for biogas fermentation (claimed).    ADVANTAGE - The composition improves marsh gas production rate by 26%, and increases the content of the methane by more than 30% at marsh gas fermentation time of 5-8 hours.
NOVELTY - Improving urban organic garbage mixed anaerobic digestion directional hydrolytic acidification effect involves mixing different urban raw organic biomass materials in ratio of 1:10 to 1:3, at organic feed loading rate of 30-60 g/l total solid (TS), and 25.8-51.6 g/l volatile solid (VS); inoculating by anaerobic sludge, and subjecting to anaerobic digestion hydrolytic acidification treatment at 35-55 degrees C; controlling pH at 4.6-6.2, where the anaerobic digestion process is for 6-9 days so as to control a component oriented into ethanol and acetic acid.    USE - For improving urban organic garbage mixed anaerobic digestion directional hydrolysis acidification effect (claimed).    ADVANTAGE - The method is simple in technology and high in operability; various biomass wastes such as kitchen garbage and garbage, sludge are simultaneously treated by an anaerobic acidification technique; appropriate proportioning of the different raw materials contributes to a yield of total organic acid of 72% higher than that of organic acid not subjected to directional acidification; alcohol and acetic acid account for 98%; and quality raw materials can be provided for organic acid production, and subsequent methanation treatment of organic acid and two phase anaerobic digestion.
NOVELTY - A method for improving kitchen garbage and storing ethanol fermentation yield involves pre-processing kitchen waste, where the kitchen garbage is kept at 40 degrees C under anaerobic condition for 1-2 days to form waste slurry having lactic acid bacteria, saccharifying for 3-6 hours at 50-60 degrees C to form kitchen waste slurry, after solid-liquid separation, leaving the saccharified kitchen waste, adding 15-25 of the pre-obtained immobilized lactic acid oxidase to the kitchen garbage, reacting at 50-60 degrees C, reacting for 3-6 hours, cooling, and carrying out alcohol fermentation.    USE - As method for improving the kitchen garbage and storing the ethanol fermentation yield (claimed).    ADVANTAGE - The method saves kitchen garbage; produces lactic acid into pyruvic acid; and improves ethanol yield of 10-20%.    DETAILED DESCRIPTION - A method for improving the kitchen garbage and storing the ethanol fermentation yield involves pre-processing the kitchen waste, where the kitchen garbage is kept at 40 degrees C under anaerobic condition for 1-2 days to obtain waste slurry containing lactic acid bacteria, saccharifying for 3-6 hours at 50-60 degrees C to obtain kitchen waste slurry, after solid-liquid separation, leaving the saccharified kitchen waste, adding 15-25 of the pre-obtained immobilized lactic acid oxidase to the kitchen garbage, reacting at 50-60 degrees C, where the saccharified liquid pH value is 5-7.2, reacting for 3-6 hours, cooling to 35-40 degrees C, and carrying out alcohol fermentation.
NOVELTY - A hydrogen generating apparatus (1) comprises hydrogen generator which generates fuel gas which has hydrogen as main component from source gas, hydrodesulfurization device (3) which is filled with hydrodesulfurization agent (19) that removes sulfur compound in source gas by hydrodesulfurization, external insulation material (17) which covers hydrogen generator and hydrodesulfurization device, internal insulation material (18) which is arranged between hydrogen generator and hydrodesulfurization device, and convection section which convects gas.    USE - A hydrogen generating apparatus (claimed).    ADVANTAGE - Temperature distribution of the whole hydrodesulfurization agent is small, thus, usage amount of hydrodesulfurization agent is minimized.    DETAILED DESCRIPTION - A hydrogen generating apparatus (1) comprises hydrogen generator which generates fuel gas which has hydrogen as main component from source gas, hydrodesulfurization device (3) which is filled with hydrodesulfurization agent (19) that removes sulfur compound in source gas by hydrodesulfurization, external insulation material (17) which covers hydrogen generator and hydrodesulfurization device, internal insulation material (18) which is arranged between hydrogen generator and hydrodesulfurization device, and convection section which convects gas and is provided between hydrogen generator and internal insulation materials, between hydrodesulfurization device and internal insulation materials, and between hydrodesulfurization device and external insulation materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Hydrogen generating apparatus (1)    Hydrodesulfurization device (3)    External insulation material (17)    Internal insulation material (18)    Hydrodesulfurization agent (19)
NOVELTY - A hydrogen generating apparatus (10) comprises desulfurization part (1) which makes sulfur compound in supplied source gas react with hydrogen and removes it, modification part (2) which produces reformed gas containing hydrogen from water, carbon monoxide removal part (3) which reduces carbon monoxide in reformed gas and produces generated gas, heater (6) which heats desulfurization part, and controller (8).    USE - A hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The hydrogen generating apparatus maintains excellent desulfurization performance, suppresses catalyst deterioration, and continuously works without reducing the amount of generated hydrogen.    DETAILED DESCRIPTION - A hydrogen generating apparatus (10) comprises desulfurization part (1) which makes sulfur compound in supplied source gas react with hydrogen and removes it, modification part (2) which produces reformed gas containing hydrogen from water, carbon monoxide (CO) removal part (3) which reduces CO in reformed gas and produces generated gas, heater (6) which heats desulfurization part, and controller (8). When factor, such as accumulation supply time when source gas is supplied, accumulation supply amount of source gas, or accumulation operation time of hydrogen generating apparatus, becomes more than threshold value, heater is controlled so that temperature of desulfurization part becomes high. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Desulfurization part (1)    Modification part (2)    Carbon monoxide removal part (3)    Heater (6)    Controller (8)    Hydrogen generating apparatus (10)
NOVELTY - Carbon monoxide (CO) from carbon dioxide (CO2) gas in hydrogen production system is reduced by steam-reforming hydrocarbon fuel from steam reforming device (1) in CO-modifying device (2), using CO selective-oxidation catalyst in CO removal device, selectively oxidizing CO in separated-and-recovered CO2 gas which is an off gas passed through CO2-pressure swing adsorption (PSA) apparatus (4) by using oxygen, and removing CO impurity to ppm order. Hydrogen production system is equipped with hydrogen PSA apparatus (3), CO2-PSA apparatus, CO removal device, and CO2 gas-liquefaction apparatus.    USE - A carbon monoxide reduction method from carbon dioxide gas in hydrogen production system (claimed).    ADVANTAGE - Oxidation removal of CO can be carried out completely, and CO selective-oxidation catalyst is effective and has prolonged performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon monoxide (CO) reduction system from carbon dioxide (CO2) gas in hydrogen production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen production method. (Drawing includes non-English language text).    Steam reforming device (1)    CO-modifying device (2)    Hydrogen PSA apparatus (3)    Carbon-dioxide-PSA apparatus (4)
NOVELTY - Manufacture of biofuel involves fermenting raw material supplied into a fermenter by microorganisms. The fermentation state of the raw material in the fermenter is controlled using a neural network.    USE - Manufacture of biofuel (claimed).    ADVANTAGE - The method efficiently, economically and stably provides biofuel, by optimizing stage in maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic structure of neural network. (Drawing includes non-English language text)    Hidden layer (A)    Output layer (R)    Input layer (S)
NOVELTY - The electrolysis cell (1) has partition (30) which is arranged between anode chamber (10) and cathode chamber (20). An anode side electrolyte solution supply unit (104) is provided to supply electrolyte solution to anode chamber. A cathode side electrolyte solution supply unit (204) is provided to supply electrolyte solution to cathode chamber. An anode side electrolyte solution exit unit is arranged in anode chamber interior. A joint pipe (1042) is provided to connect inlet port (1043) and distribution pipe (1041).    USE - Electrolysis cell of bipolar electrolytic cell (claimed), for electrolyzing alkali metal chloride aqueous solution e.g. salt solution and manufacturing high concentration alkali metal hydroxide, hydrogen, and chlorine.    ADVANTAGE - The joint pipe is provided to the connect inlet port and distribution pipe, so that the electrolyte solution is not remained in the electrolysis cell while discharging electrolyte solution at the time of electrolysis stop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the electrolysis cell.    Electrolysis cell (1)    Anode chamber (10)    Cathode chamber (20)    Partition (30)    Anode side electrolyte solution supply unit (104)    Cathode side electrolyte solution supply unit (204)    Distribution pipe (1041)    Joint pipe (1042)    Inlet port (1043)
NOVELTY - The diaphragm is provided with sheet-like porous support portion and microporous film (2) containing organic polymer resin. The microporous film is laminated on the single surface or both surfaces of porous support portion. The film surface of microporous film that contacts porous support portion is set as desired surface (B) while the film surface formed on opposite side to desired surface is set as other surface (A) by satisfying predetermined relation repressing Pa as average hole diameter in desired surface and Pb as average hole diameter in other surface.    USE - Diaphragm for alkaline water electrolysis of alkaline-water-electrolysis apparatus (claimed) used for manufacturing hydrogen used in petroleum refining industry, chemosynthesis material, metal purification process, home-use cogeneration system and fuel cell electric vehicle.    ADVANTAGE - Since the film surface of microporous film that contacts porous support portion is set as desired surface while the film surface formed on opposite side to desired surface is set as other surface by satisfying predetermined relation repressing, the gas-barrier property can be maintained and the diaphragm for alkaline water electrolysis can be provided with high ionic permeability even if physical damage arises on the film surface.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an alkaline-water-electrolysis apparatus; and    (2) a manufacturing method of diaphragm for alkaline water electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the microporous film.    Microporous film (2)    Film surfaces (A,B)    Average hole diameter in desired surface (Pa)    Average hole diameter in other surface (Pb)
NOVELTY - The apparatus (40) has a movable frame (20) that is moved to drive a rail (14) in waste material installation area (13) containing organic waste. A rotation unit (30) is mounted in the movable frame, for stirring the organic waste by a rotational drive. A rotating shaft (31) of rotation unit is supported by the movable frame in the upper direction of a bottom wall portion (11) during horizontal suspension state. An extension element (32) of rotation unit is extended from an outer periphery of rotating shaft, and is bent along the longitudinal direction.    USE - Movable stirring apparatus for organic waste stirring processing apparatus (claimed), for stirring organic waste such as sludge of excrement discharged from livestock, organic refuse discharged from home and sewage.    ADVANTAGE - Since the extension element of the rotation unit is bent along the longitudinal direction, the organic waste in waste material installation area can be stirred effectively without rotationally driving the rotation unit. The need for installing lifting and lowering apparatus to raise/lower the rotation unit with respect to movable frame can be avoided. The cost of movable stirring apparatus can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic waste stirring processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional side view of the movable stirring apparatus and organic waste stirring processing apparatus.    Bottom wall portion (11)    Waste material installation area (13)    Rail (14)    Movable frame (20)    Rotation unit (30)    Rotating shaft (31)    Extension element (32)    Movable stirring apparatus (40)